TWI686233B - Runner system with high temperature desorption and its method - Google Patents

Runner system with high temperature desorption and its method Download PDF

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Publication number
TWI686233B
TWI686233B TW107138326A TW107138326A TWI686233B TW I686233 B TWI686233 B TW I686233B TW 107138326 A TW107138326 A TW 107138326A TW 107138326 A TW107138326 A TW 107138326A TW I686233 B TWI686233 B TW I686233B
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Taiwan
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gas
desorption
adsorption
pipeline
runner
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TW107138326A
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Chinese (zh)
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TW202015790A (en
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鄭石治
扶亞民
劉邦昱
洪守銘
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華懋科技股份有限公司
大陸商上海華懋環保節能設備有限公司
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Priority to TW107138326A priority Critical patent/TWI686233B/en
Priority to CN201910013813.7A priority patent/CN111111382A/en
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Publication of TWI686233B publication Critical patent/TWI686233B/en
Publication of TW202015790A publication Critical patent/TW202015790A/en

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/06—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/40—Further details for adsorption processes and devices
    • B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
    • B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
    • B01D2259/4009—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating using hot gas

Abstract

本發明為一種具高溫脫附之轉輪系統及其方法，主要係用來進行在線運轉(ON LINE)時，除了能進行高溫脫附外，還能將所殘留的高沸點有機物(VOC)進行脫出，讓該吸附轉輪能恢復其吸附能力，而增加揮發性有機廢氣的處理效能，並達到減少污染物排放之效果。 The present invention is a runner system with high temperature desorption and its method. It is mainly used for online operation (ON LINE). In addition to high temperature desorption, it can also carry out residual high boiling point organic matter (VOC). Withdrawing, the adsorption rotor can restore its adsorption capacity, increase the treatment efficiency of volatile organic waste gas, and achieve the effect of reducing pollutant emissions.

Description

具高溫脫附之轉輪系統及其方法 Runner system with high temperature desorption and its method

本發明係有關於一種具高溫脫附之轉輪系統及其方法，尤指一種使增加有機廢氣處理效能，而適用於半導體產業、光電產業或化學相關產業之廠房的廢氣處理。 The invention relates to a runner system with high temperature desorption and a method thereof, in particular to an exhaust gas treatment for increasing the efficiency of organic waste gas treatment, which is suitable for factories in the semiconductor industry, optoelectronic industry or chemical related industries.

目前在半導體產業或光電產業的製造生產過程中都會產生具有揮發性有機氣體(VOC)，因此，在各廠區都會安裝處理揮發性有機氣體(VOC)的處理設備，以避免揮發性有機氣體(VOC)直接排入空氣中而造成空氣污染。 At present, volatile organic gas (VOC) is produced in the manufacturing process of the semiconductor industry or the optoelectronic industry. Therefore, processing equipment for processing volatile organic gas (VOC) is installed in each plant to avoid volatile organic gas (VOC) ) Directly discharged into the air causing air pollution.

而，目前在廠區安裝處理揮發性有機氣體(VOC)的處理設備大多採用吸附轉輪方式來吸附揮發性有機氣體(VOC)，但在使用一段時間後，常有高沸點物質不易脫附而殘留於吸附轉輪上，直接影響了吸附轉輪的吸附效能，因此，目前處理方式都是委托外面專業廠商來定期進行洗滌吸附轉輪，以確保吸附轉輪的運作效率和氣流流暢度。 However, at present, most of the processing equipment installed in the factory area for processing volatile organic gas (VOC) uses an adsorption rotor to adsorb volatile organic gas (VOC), but after a period of use, there are often high-boiling substances that are not easy to desorb and remain The adsorption rotor directly affects the adsorption performance of the adsorption rotor. Therefore, the current treatment method is to entrust an external professional manufacturer to periodically wash the adsorption rotor to ensure the operation efficiency and airflow smoothness of the adsorption rotor.

但，上述的定期進行洗滌吸附轉輪時，都需要使用大量的清水來進行清洗，也因此產生大量含有揮發性有機氣體(VOC)之廢水，而此時含有揮發性有機氣體(VOC)之廢水中的化學需氧量(COD)非常高，無法直接由廠內廢水處理系統處理後放流，須委托專業合格廢棄物清運公司來進行處理才行。 However, the above-mentioned regular washing of the adsorption runner requires the use of a large amount of clean water for cleaning, and therefore a large amount of wastewater containing volatile organic gas (VOC) is generated, and at this time the wastewater containing volatile organic gas (VOC) The Chemical Oxygen Demand (COD) is very high and cannot be directly discharged by the wastewater treatment system in the plant, and it must be entrusted to a professional qualified waste removal and transportation company for treatment.

因此，本發明人有鑑於上述缺失，期能提出一種具有高溫脫附之效能的具高溫脫附之轉輪系統及其方法，令使用者可輕易操作組裝，乃潛心研思、設計組製，以提供使用者便利性，為本發明人所欲研發之發明動機者。 Therefore, in view of the above deficiencies, the inventor hopes to propose a high-temperature desorption rotor system with high-temperature desorption and its method, so that the user can easily operate the assembly, and is devoted to deliberate and design the system. In order to provide user convenience, it is the motive of the invention that the inventor intends to develop.

本發明之主要目的，在於提供一種具高溫脫附之轉輪系統及其方法，主要係用來進行在線運轉(ON LINE)時，除了能進行高溫脫附外，還能將所殘留的高沸點有機物(VOC)進行脫出，讓該吸附轉輪能恢復其吸附能力，而增加揮發性有機廢氣的處理效能，並達到減少污染物排放之效果，進而增加整體之實用性者。 The main purpose of the present invention is to provide a runner system with high temperature desorption and its method, which is mainly used for online operation (ON LINE), in addition to high temperature desorption, it can also remove the remaining high boiling point The organic matter (VOC) is removed, so that the adsorption rotor can restore its adsorption capacity, increase the treatment efficiency of volatile organic waste gas, and achieve the effect of reducing pollutant emissions, thereby increasing the overall practicality.

本發明之另一目的，在於提供一種具高溫脫附之轉輪系統及其方法，透過將進入高溫脫附區的高溫熱氣能再提升到一定溫度(例如300℃)，使該吸附轉輪能擁有更高溫度之熱氣的輸入，讓整體的處理效能由以往的95%提昇至97%以上，進而增加整體之使用性者。 Another object of the present invention is to provide a runner system with high-temperature desorption and a method thereof, by raising the high-temperature hot gas energy entering the high-temperature desorption zone to a certain temperature (for example, 300°C) to make the adsorption runner energy With the input of hot air at a higher temperature, the overall processing efficiency has been increased from 95% to 97%, which in turn increases the overall usability.

本發明之再一目的，在於提供一種具高溫脫附之轉輪系統及其方法，透過該吸附轉輪的一側與另一側所連接的管路及裝置能呈相同方向或是呈相反方向，以讓該吸附轉輪能具有不同的排列組合的效能，進而增加整體之操作性者。 Still another object of the present invention is to provide a runner system with high temperature desorption and a method thereof. The pipes and devices connected to one side and the other side through the adsorption runner can be in the same direction or in opposite directions , So that the suction runner can have different permutations and combinations of performance, thereby increasing the overall operability.

為了能夠更進一步瞭解本發明之特徵、特點和技術內容，請參閱以下有關本發明之詳細說明與附圖，惟所附圖式僅提供參考與說明用，非用以限制本發明。 In order to further understand the features, characteristics and technical contents of the present invention, please refer to the following detailed description and drawings of the present invention, but the drawings are provided for reference and explanation only, and are not intended to limit the present invention.

A‧‧‧一側 A‧‧‧side

B‧‧‧另一側 B‧‧‧The other side

100‧‧‧焚燒裝置 100‧‧‧Incinerator

101‧‧‧入口 101‧‧‧ entrance

102‧‧‧出口 102‧‧‧Export

110‧‧‧第一吸附轉輪 110‧‧‧The first adsorption runner

1101‧‧‧吸附區 1101‧‧‧Adsorption zone

1102‧‧‧冷卻區 1102‧‧‧cooling zone

1103‧‧‧脫附區 1103‧‧‧Desorption zone

1104‧‧‧高溫脫附區 1104‧‧‧High temperature desorption zone

111‧‧‧廢氣進氣管路 111‧‧‧ Exhaust gas inlet line

112‧‧‧第一淨氣排放管路 112‧‧‧The first clean gas discharge line

113‧‧‧第一冷卻氣進氣管路 113‧‧‧The first cooling air intake line

114‧‧‧第一冷卻氣輸送管路 114‧‧‧ First cooling gas delivery pipeline

115‧‧‧第一熱氣輸送管路 115‧‧‧The first hot gas delivery pipeline

116‧‧‧第一脫附濃縮氣體管路 116‧‧‧The first desorption concentrated gas pipeline

1161‧‧‧風機 1161‧‧‧Fan

117‧‧‧第二熱氣輸送管路 117‧‧‧Second hot gas delivery pipeline

118‧‧‧第一高溫脫附濃縮氣體管路 118‧‧‧The first high temperature desorption concentrated gas pipeline

120‧‧‧第二吸附轉輪 120‧‧‧Second adsorption runner

1201‧‧‧吸附區 1201‧‧‧Adsorption zone

1202‧‧‧冷卻區 1202‧‧‧cooling area

1203‧‧‧脫附區 1203‧‧‧Desorption zone

1204‧‧‧高溫脫附區 1204‧‧‧High temperature desorption zone

121‧‧‧第二淨氣排放管路 121‧‧‧Second clean gas discharge line

1211‧‧‧風機 1211‧‧‧Fan

122‧‧‧第二冷卻氣進氣管路 122‧‧‧Second cooling air intake line

123‧‧‧第二冷卻氣輸送管路 123‧‧‧ Second cooling gas delivery pipeline

124‧‧‧第三熱氣輸送管路 124‧‧‧The third hot gas delivery pipeline

125‧‧‧第二脫附濃縮氣體管路 125‧‧‧Second desorption concentrated gas pipeline

1251‧‧‧風機 1251‧‧‧Fan

126‧‧‧第四熱氣輸送管路 126‧‧‧The fourth hot gas delivery pipeline

127‧‧‧第二高溫脫附濃縮氣體管路 127‧‧‧Second high-temperature desorption concentrated gas pipeline

130‧‧‧第一加熱裝置 130‧‧‧First heating device

140‧‧‧第二加熱裝置 140‧‧‧Second heating device

150‧‧‧第三加熱裝置 150‧‧‧The third heating device

160‧‧‧第四加熱裝置 160‧‧‧The fourth heating device

170‧‧‧煙囪 170‧‧‧Chimney

181‧‧‧廢氣連通管路 181‧‧‧ Waste gas communication pipeline

1811‧‧‧廢氣連通控制閥門 1811‧‧‧ Exhaust gas connection control valve

182‧‧‧第一淨氣連通管路 182‧‧‧The first clean gas communication pipeline

1821‧‧‧第一淨氣連通控制閥門 1821‧‧‧The first clean gas communication control valve

191‧‧‧第一熱氣旁通管路 191‧‧‧The first hot gas bypass line

1911‧‧‧第一熱氣旁通控制閥門 1911‧‧‧The first hot gas bypass control valve

192‧‧‧第三熱氣旁通管路 192‧‧‧The third hot gas bypass line

1921‧‧‧第三熱氣旁通控制閥門 1921‧‧‧The third hot gas bypass control valve

200‧‧‧焚燒裝置 200‧‧‧Incinerator

201‧‧‧入口 201‧‧‧ Entrance

202‧‧‧出口 202‧‧‧Export

210‧‧‧第一吸附轉輪 210‧‧‧The first adsorption runner

2101‧‧‧吸附區 2101‧‧‧Adsorption zone

2102‧‧‧冷卻區 2102‧‧‧cooling zone

2103‧‧‧脫附區 2103‧‧‧Desorption zone

2104‧‧‧高溫脫附區 2104‧‧‧High temperature desorption zone

211‧‧‧廢氣進氣管路 211‧‧‧Exhaust gas inlet line

212‧‧‧第一淨氣排放管路 212‧‧‧The first clean gas discharge line

213‧‧‧第一冷卻氣進氣管路 213‧‧‧ The first cooling gas intake line

214‧‧‧第一冷卻氣輸送管路 214‧‧‧ First cooling gas delivery pipeline

215‧‧‧第一熱氣輸送管路 215‧‧‧The first hot gas delivery pipeline

216‧‧‧第一脫附濃縮氣體管路 216‧‧‧The first desorption concentrated gas pipeline

2161‧‧‧風機 2161‧‧‧Fan

217‧‧‧第二熱氣輸送管路 217‧‧‧ Second hot gas delivery pipeline

218‧‧‧第一高溫脫附濃縮氣體管路 218‧‧‧The first high-temperature desorption concentrated gas pipeline

220‧‧‧第二吸附轉輪 220‧‧‧Second adsorption runner

2201‧‧‧吸附區 2201‧‧‧Adsorption zone

2202‧‧‧冷卻區 2202‧‧‧cooling zone

2203‧‧‧脫附區 2203‧‧‧Desorption zone

2204‧‧‧高溫脫附區 2204‧‧‧High temperature desorption zone

221‧‧‧第二淨氣排放管路 221‧‧‧Second clean gas discharge line

2211‧‧‧風機 2211‧‧‧Fan

222‧‧‧第二冷卻氣進氣管路 222‧‧‧ Second cooling gas inlet line

223‧‧‧第二冷卻氣輸送管路 223‧‧‧Second cooling gas delivery pipeline

224‧‧‧第三熱氣輸送管路 224‧‧‧The third hot gas delivery pipeline

225‧‧‧第二脫附濃縮氣體管路 225‧‧‧Second desorbed concentrated gas pipeline

2251‧‧‧風機 2251‧‧‧Fan

226‧‧‧第四熱氣輸送管路 226‧‧‧The fourth hot gas delivery pipeline

227‧‧‧第二高溫脫附濃縮氣體管路 227‧‧‧Second high-temperature desorption concentrated gas pipeline

230‧‧‧第一加熱裝置 230‧‧‧First heating device

240‧‧‧第二加熱裝置 240‧‧‧Second heating device

250‧‧‧第三加熱裝置 250‧‧‧The third heating device

260‧‧‧第四加熱裝置 260‧‧‧The fourth heating device

270‧‧‧煙囪 270‧‧‧Chimney

282‧‧‧第一淨氣連通管路 282‧‧‧The first clean gas communication line

2821‧‧‧第一淨氣連通控制閥門 2821‧‧‧The first clean gas communication control valve

283‧‧‧第二淨氣連通管路 283‧‧‧The second clean gas communication pipeline

2831‧‧‧第二淨氣連通控制閥門 2831‧‧‧Second clean gas communication control valve

291‧‧‧第一熱氣旁通管路 291‧‧‧The first hot gas bypass line

2911‧‧‧第一熱氣旁通控制閥門 2911‧‧‧The first hot gas bypass control valve

292‧‧‧第三熱氣旁通管路 292‧‧‧The third hot gas bypass line

2921‧‧‧第三熱氣旁通控制閥門 2921‧‧‧The third hot gas bypass control valve

300‧‧‧焚燒裝置 300‧‧‧Incinerator

301‧‧‧入口 301‧‧‧ entrance

302‧‧‧出口 302‧‧‧Export

310‧‧‧第一吸附轉輪 310‧‧‧The first adsorption runner

3101‧‧‧吸附區 3101‧‧‧Adsorption zone

3102‧‧‧冷卻區 3102‧‧‧cooling zone

3103‧‧‧脫附區 3103‧‧‧Desorption zone

3104‧‧‧高溫脫附區 3104‧‧‧High temperature desorption zone

311‧‧‧廢氣進氣管路 311‧‧‧ Exhaust gas inlet line

312‧‧‧第一淨氣排放管路 312‧‧‧The first clean gas discharge line

313‧‧‧第一冷卻氣進氣管路 313‧‧‧The first cooling gas intake line

314‧‧‧第一冷卻氣輸送管路 314‧‧‧ First cooling gas delivery pipeline

315‧‧‧第一熱氣輸送管路 315‧‧‧The first hot gas delivery pipeline

316‧‧‧第一脫附濃縮氣體管路 316‧‧‧The first desorption concentrated gas pipeline

3161‧‧‧風機 3161‧‧‧Fan

317‧‧‧第二熱氣輸送管路 317‧‧‧The second hot gas delivery pipeline

318‧‧‧第一高溫脫附濃縮氣體管路 318‧‧‧The first high temperature desorption concentrated gas pipeline

320‧‧‧第二吸附轉輪 320‧‧‧Second adsorption runner

3201‧‧‧吸附區 3201‧‧‧Adsorption zone

3202‧‧‧冷卻區 3202‧‧‧cooling area

3203‧‧‧脫附區 3203‧‧‧Desorption zone

3204‧‧‧高溫脫附區 3204‧‧‧High temperature desorption zone

321‧‧‧第二淨氣排放管路 321‧‧‧Second clean gas discharge line

3211‧‧‧風機 3211‧‧‧Fan

322‧‧‧第二冷卻氣進氣管路 322‧‧‧Second cooling air intake line

323‧‧‧第二冷卻氣輸送管路 323‧‧‧Second cooling gas delivery pipeline

324‧‧‧第三熱氣輸送管路 324‧‧‧The third hot gas delivery pipeline

325‧‧‧第二脫附濃縮氣體管路 325‧‧‧Second desorbed concentrated gas pipeline

3251‧‧‧風機 3251‧‧‧Fan

326‧‧‧第四熱氣輸送管路 326‧‧‧The fourth hot gas delivery pipeline

327‧‧‧第二高溫脫附濃縮氣體管路 327‧‧‧Second high-temperature desorption concentrated gas pipeline

330‧‧‧第一加熱裝置 330‧‧‧First heating device

340‧‧‧第二加熱裝置 340‧‧‧Second heating device

350‧‧‧第三加熱裝置 350‧‧‧The third heating device

360‧‧‧第四加熱裝置 360‧‧‧The fourth heating device

370‧‧‧煙囪 370‧‧‧Chimney

381‧‧‧廢氣連通管路 381‧‧‧ Waste gas communication pipeline

3811‧‧‧廢氣連通控制閥門 3811‧‧‧ Waste gas communication control valve

383‧‧‧第二淨氣連通管路 383‧‧‧The second clean gas communication line

3831‧‧‧第二淨氣連通控制閥門 3831‧‧‧Second clean gas communication control valve

391‧‧‧第一熱氣旁通管路 391‧‧‧The first hot gas bypass line

3911‧‧‧第一熱氣旁通控制閥門 3911‧‧‧The first hot gas bypass control valve

392‧‧‧第三熱氣旁通管路 392‧‧‧The third hot gas bypass line

3921‧‧‧第三熱氣旁通控制閥門 3921‧‧‧The third hot gas bypass control valve

400‧‧‧焚燒裝置 400‧‧‧Incinerator

401‧‧‧入口 401‧‧‧ entrance

402‧‧‧出口 402‧‧‧Export

410‧‧‧第一吸附轉輪 410‧‧‧The first adsorption runner

4101‧‧‧吸附區 4101‧‧‧Adsorption zone

4102‧‧‧冷卻區 4102‧‧‧cooling area

4103‧‧‧脫附區 4103‧‧‧Desorption zone

4104‧‧‧高溫脫附區 4104‧‧‧High temperature desorption zone

411‧‧‧廢氣進氣管路 411‧‧‧Exhaust gas inlet line

412‧‧‧第一淨氣排放管路 412‧‧‧The first clean gas discharge line

413‧‧‧第一冷卻氣進氣管路 413‧‧‧The first cooling air intake line

414‧‧‧第一冷卻氣輸送管路 414‧‧‧The first cooling gas delivery pipeline

415‧‧‧第一熱氣輸送管路 415‧‧‧The first hot gas delivery pipeline

416‧‧‧第一脫附濃縮氣體管路 416‧‧‧The first desorption concentrated gas pipeline

4161‧‧‧風機 4161‧‧‧Fan

417‧‧‧第二熱氣輸送管路 417‧‧‧The second hot gas delivery pipeline

418‧‧‧第一高溫脫附濃縮氣體管路 418‧‧‧The first high-temperature desorption concentrated gas pipeline

420‧‧‧第二吸附轉輪 420‧‧‧Second adsorption runner

4201‧‧‧吸附區 4201‧‧‧Adsorption zone

4202‧‧‧冷卻區 4202‧‧‧cooling area

4203‧‧‧脫附區 4203‧‧‧Desorption zone

4204‧‧‧高溫脫附區 4204‧‧‧High temperature desorption zone

421‧‧‧第二淨氣排放管路 421‧‧‧Second clean gas discharge line

4211‧‧‧風機 4211‧‧‧Fan

422‧‧‧第二冷卻氣進氣管路 422‧‧‧Second cooling air intake line

423‧‧‧第二冷卻氣輸送管路 423‧‧‧Second cooling gas delivery pipeline

424‧‧‧第三熱氣輸送管路 424‧‧‧The third hot gas delivery pipeline

425‧‧‧第二脫附濃縮氣體管路 425‧‧‧Second desorbed concentrated gas pipeline

4251‧‧‧風機 4251‧‧‧Fan

426‧‧‧第四熱氣輸送管路 426‧‧‧The fourth hot gas delivery pipeline

427‧‧‧第二高溫脫附濃縮氣體管路 427‧‧‧Second high-temperature desorption concentrated gas pipeline

430‧‧‧第一加熱裝置 430‧‧‧First heating device

440‧‧‧第二加熱裝置 440‧‧‧Second heating device

450‧‧‧第三加熱裝置 450‧‧‧The third heating device

460‧‧‧第四加熱裝置 460‧‧‧The fourth heating device

470‧‧‧煙囪 470‧‧‧Chimney

484‧‧‧第一淨氣第一連通管路 484‧‧‧First clean gas first communication line

4841‧‧‧第一淨氣第一連通控制閥門 4841‧‧‧The first clean gas first communication control valve

485‧‧‧第一淨氣第二連通管路 485‧‧‧The first clean gas second communication line

4851‧‧‧第一淨氣第二連通控制閥門 4851‧‧‧The first clean gas second communication control valve

491‧‧‧第一熱氣旁通管路 491‧‧‧The first hot gas bypass line

4911‧‧‧第一熱氣旁通控制閥門 4911‧‧‧The first hot gas bypass control valve

492‧‧‧第三熱氣旁通管路 492‧‧‧The third hot gas bypass line

4921‧‧‧第三熱氣旁通控制閥門 4921‧‧‧The third hot gas bypass control valve

500‧‧‧焚燒裝置 500‧‧‧Incinerator

501‧‧‧入口 501‧‧‧ entrance

502‧‧‧出口 502‧‧‧Export

510‧‧‧吸附轉輪 510‧‧‧Adsorption rotor

5101‧‧‧吸附區 5101‧‧‧Adsorption zone

5102‧‧‧冷卻區 5102‧‧‧cooling area

5103‧‧‧脫附區 5103‧‧‧Desorption zone

5104‧‧‧高溫脫附區 5104‧‧‧High temperature desorption zone

511‧‧‧廢氣進氣管路 511‧‧‧ exhaust gas inlet line

512‧‧‧淨氣排放管路 512‧‧‧ Pure gas discharge pipeline

5121‧‧‧風機 5121‧‧‧Fan

513‧‧‧冷卻氣進氣管路 513‧‧‧ Cooling gas inlet line

514‧‧‧冷卻氣輸送管路 514‧‧‧cooling gas delivery pipeline

515‧‧‧第一熱氣輸送管路 515‧‧‧The first hot gas delivery pipeline

516‧‧‧脫附濃縮氣體管路 516‧‧‧Desorption concentrated gas pipeline

5161‧‧‧風機 5161‧‧‧Fan

517‧‧‧第二熱氣輸送管路 517‧‧‧Second hot gas delivery pipeline

518‧‧‧高溫脫附濃縮氣體管路 518‧‧‧High temperature desorption concentrated gas pipeline

520‧‧‧第一加熱裝置 520‧‧‧First heating device

530‧‧‧第二加熱裝置 530‧‧‧Second heating device

570‧‧‧煙囪 570‧‧‧Chimney

581‧‧‧廢氣連通管路 581‧‧‧ Waste gas communication pipeline

5811‧‧‧廢氣連通控制閥門 5811‧‧‧ Waste gas communication control valve

591‧‧‧熱氣旁通管路 591‧‧‧Hot gas bypass line

5911‧‧‧熱氣旁通控制閥門 5911‧‧‧Hot gas bypass control valve

600‧‧‧焚燒裝置 600‧‧‧Incinerator

601‧‧‧入口 601‧‧‧ entrance

602‧‧‧出口 602‧‧‧Export

610‧‧‧吸附轉輪 610‧‧‧Adsorption rotor

6101‧‧‧吸附區 6101‧‧‧Adsorption zone

6102‧‧‧冷卻區 6102‧‧‧cooling zone

6103‧‧‧脫附區 6103‧‧‧Desorption zone

6104‧‧‧高溫脫附區 6104‧‧‧High temperature desorption zone

611‧‧‧廢氣進氣管路 611‧‧‧ Exhaust gas inlet line

612‧‧‧淨氣排放管路 612‧‧‧ net gas discharge pipeline

6121‧‧‧風機 6121‧‧‧Fan

613‧‧‧冷卻氣進氣管路 613‧‧‧cooling air intake line

614‧‧‧冷卻氣輸送管路 614‧‧‧cooling gas pipeline

615‧‧‧第一熱氣輸送管路 615‧‧‧The first hot gas delivery pipeline

616‧‧‧脫附濃縮氣體管路 616‧‧‧Desorption concentrated gas pipeline

6161‧‧‧風機 6161‧‧‧Fan

617‧‧‧第二熱氣輸送管路 617‧‧‧The second hot gas delivery pipeline

618‧‧‧高溫脫附濃縮氣體管路 618‧‧‧High temperature desorption concentrated gas pipeline

620‧‧‧第一加熱裝置 620‧‧‧First heating device

630‧‧‧第二加熱裝置 630‧‧‧Second heating device

670‧‧‧煙囪 670‧‧‧Chimney

682‧‧‧淨氣連通管路 682‧‧‧Clean gas communication pipeline

6821‧‧‧淨氣連通控制閥門 6821‧‧‧Clean gas connection control valve

691‧‧‧熱氣旁通管路 691‧‧‧Hot gas bypass line

6911‧‧‧熱氣旁通控制閥門 6911‧‧‧ Hot gas bypass control valve

S100‧‧‧輸入待吸附之氣體 S100‧‧‧Enter the gas to be adsorbed

S110‧‧‧輸入用來冷卻之氣體 S110‧‧‧Enter the gas used for cooling

S120‧‧‧輸送高溫熱氣進行脫附 S120‧‧‧Delivering high temperature hot gas for desorption

S130‧‧‧再將高沸點有機物脫出 S130‧‧‧Remove high-boiling organic matter

S140‧‧‧輸送欲再吸附之氣體 S140‧‧‧Transport the gas to be re-adsorbed

S150‧‧‧輸入用來冷卻之氣體 S150‧‧‧Enter the gas used for cooling

S160‧‧‧輸送高溫熱氣進行脫附 S160‧‧‧Transport high temperature hot gas for desorption

S170‧‧‧再將高沸點有機物脫出 S170‧‧‧Remove high-boiling organic matter

S200‧‧‧輸入待吸附之氣體 S200‧‧‧Enter the gas to be adsorbed

S210‧‧‧輸入用來冷卻之氣體 S210‧‧‧Enter the gas used for cooling

S220‧‧‧輸送高溫熱氣進行脫附 S220‧‧‧Delivering high temperature hot gas for desorption

S230‧‧‧再將高沸點有機物脫出 S230‧‧‧Remove high-boiling organic matter

S240‧‧‧輸送欲再吸附之氣體 S240‧‧‧Convey gas to be re-adsorbed

S250‧‧‧輸入用來冷卻之氣體 S250‧‧‧Enter the gas used for cooling

S260‧‧‧輸送高溫熱氣進行脫附 S260‧‧‧Delivering high temperature hot gas for desorption

S270‧‧‧再將高沸點有機物脫出 S270‧‧‧Remove high-boiling organic matter

S300‧‧‧輸入待吸附之氣體 S300‧‧‧Enter the gas to be adsorbed

S310‧‧‧輸入用來冷卻之氣體 S310‧‧‧Enter the gas used for cooling

S320‧‧‧輸送高溫熱氣進行脫附 S320‧‧‧Delivering high temperature hot gas for desorption

S330‧‧‧再將高沸點有機物脫出 S330‧‧‧Remove high-boiling organic matter

S340‧‧‧輸送欲再吸附之氣體 S340‧‧‧Convey gas to be re-adsorbed

S350‧‧‧輸入用來冷卻之氣體 S350‧‧‧Enter the gas used for cooling

S360‧‧‧輸送高溫熱氣進行脫附 S360‧‧‧Delivering high temperature hot gas for desorption

S370‧‧‧再將高沸點有機物脫出 S370‧‧‧Remove high-boiling organic matter

S400‧‧‧輸入待吸附之氣體 S400‧‧‧Enter the gas to be adsorbed

S410‧‧‧輸入用來冷卻之氣體 S410‧‧‧Enter the gas used for cooling

S420‧‧‧輸送高溫熱氣進行脫附 S420‧‧‧Delivering high temperature hot gas for desorption

S430‧‧‧再將高沸點有機物脫出 S430‧‧‧Remove high-boiling organic matter

S440‧‧‧輸送欲再吸附之氣體 S440‧‧‧Convey gas to be re-adsorbed

S450‧‧‧輸入用來冷卻之氣體 S450‧‧‧Enter the gas used for cooling

S460‧‧‧輸送高溫熱氣進行脫附 S460‧‧‧Delivering high temperature hot gas for desorption

S470‧‧‧再將高沸點有機物脫出 S470‧‧‧Remove high-boiling organic matter

S500‧‧‧輸入待吸附之氣體 S500‧‧‧Enter the gas to be adsorbed

S510‧‧‧輸入用來冷卻之氣體 S510‧‧‧Enter the gas used for cooling

S520‧‧‧輸送高溫熱氣進行脫附 S520‧‧‧Delivering high temperature hot gas for desorption

S530‧‧‧再將高沸點有機物脫出 S530‧‧‧Remove high-boiling organic matter

S600‧‧‧輸入待吸附之氣體 S600‧‧‧Enter the gas to be adsorbed

S610‧‧‧輸入用來冷卻之氣體 S610‧‧‧Enter the gas used for cooling

S620‧‧‧輸送高溫熱氣進行脫附 S620‧‧‧Delivering high temperature hot gas for desorption

S630‧‧‧再將高沸點有機物脫出 S630‧‧‧Remove high-boiling organic matter

第1圖係為本發明之第一種實施方式的主要步驟流程圖。 Figure 1 is a flowchart of the main steps of the first embodiment of the present invention.

第2圖係為本發明之第一種實施架構的主要系統架構示意圖。 Figure 2 is a schematic diagram of the main system architecture of the first implementation architecture of the present invention.

第3圖係為本發明之第一種實施架構的另一系統架構示意圖。 FIG. 3 is a schematic diagram of another system architecture of the first implementation architecture of the present invention.

第4圖係為本發明之第二種實施方式的主要步驟流程圖。 Figure 4 is a flow chart of the main steps of the second embodiment of the present invention.

第5圖係為本發明之第二種實施架構的主要系統架構示意圖。 Figure 5 is a schematic diagram of the main system architecture of the second implementation architecture of the present invention.

第6圖係為本發明之第二種實施架構的另一系統架構示意圖。 FIG. 6 is a schematic diagram of another system architecture of the second implementation architecture of the present invention.

第7圖係為本發明之第三種實施方式的主要步驟流程圖。 FIG. 7 is a flowchart of the main steps of the third embodiment of the present invention.

第8圖係為本發明之第三種實施架構的主要系統架構示意圖。 Figure 8 is a schematic diagram of the main system architecture of the third implementation architecture of the present invention.

第9圖係為本發明之第三種實施架構的另一系統架構示意圖。 FIG. 9 is a schematic diagram of another system architecture of the third implementation architecture of the present invention.

第10圖係為本發明之第四種實施方式的主要步驟流程圖。 Figure 10 is a flowchart of the main steps of the fourth embodiment of the present invention.

第11圖係為本發明之第四種實施架構的主要系統架構示意圖。 Figure 11 is a schematic diagram of the main system architecture of the fourth implementation architecture of the present invention.

第12圖係為本發明之第四種實施架構的另一系統架構示意圖。 FIG. 12 is a schematic diagram of another system architecture of the fourth implementation architecture of the present invention.

第13圖係為本發明之第五種實施方式的主要步驟流程圖。 Figure 13 is a flowchart of the main steps of the fifth embodiment of the present invention.

第14圖係為本發明之第五種實施架構的主要系統架構示意圖。 Figure 14 is a schematic diagram of the main system architecture of the fifth implementation architecture of the present invention.

第15圖係為本發明之第五種實施架構的另一系統架構示意圖。 FIG. 15 is a schematic diagram of another system architecture of a fifth implementation architecture of the present invention.

第16圖係為本發明之第六種實施方式的主要步驟流程圖。 Figure 16 is a flowchart of the main steps of the sixth embodiment of the present invention.

第17圖係為本發明之第六種實施架構的主要系統架構示意圖。 Figure 17 is a schematic diagram of the main system architecture of the sixth implementation architecture of the present invention.

第18圖係為本發明之第六種實施架構的另一系統架構示意圖。 FIG. 18 is a schematic diagram of another system architecture of the sixth implementation architecture of the present invention.

請參閱第1~18圖，係為本發明實施例之示意圖，而本發明之具高溫脫附之轉輪系統及其方法的最佳實施方式係運用於半導體產 業、光電產業或化學相關產業之廠房的廢氣處理，透過本發明之設計，以用來進行在線運轉(ON LINE)時，能將所殘留的高沸點有機廢氣(VOC)脫出，讓該吸附轉輪能恢復其吸附能力，而增加揮發性有機廢氣的處理效能，並達到減少汙染物排放之效果。 Please refer to Figures 1 to 18, which are schematic diagrams of embodiments of the present invention, and the best embodiment of the runner system and method with high temperature desorption according to the present invention is applied to semiconductor production The exhaust gas treatment of industrial plants, photoelectric industry or chemical-related industries through the design of the present invention can be used to perform online operation (ON LINE), the residual high-boiling organic waste gas (VOC) can be removed to allow the adsorption The runner can restore its adsorption capacity, increase the treatment efficiency of volatile organic waste gas, and achieve the effect of reducing pollutant emissions.

而本發明第一種實施方式的具高溫脫附之轉輪方法，主要係設有一第一吸附轉輪110、一第二吸附轉輪120、一第一加熱裝置130、一第二加熱裝置140、一第三加熱裝置150及一第四加熱裝置160，而該第一吸附轉輪110係設有吸附區1101、冷卻區1102、脫附區1103及高溫脫附區1104，另該第二吸附轉輪120係設有吸附區1201、冷卻區1202、脫附區1203及高溫脫附區1204，因此，本發明主要在於該第一吸附轉輪110及該第二吸附轉輪120除了設有吸附區1101、1201、冷卻區1102、1202及脫附區1103、1203外，還設有高溫脫附區1104、1204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪110及該第二吸附轉輪120能恢復其吸附能力，使該第一吸附轉輪110及該第二吸附轉輪120能具有四個區域。 The rotor method with high temperature desorption according to the first embodiment of the present invention is mainly provided with a first adsorption runner 110, a second adsorption runner 120, a first heating device 130, and a second heating device 140 , A third heating device 150 and a fourth heating device 160, and the first adsorption runner 110 is provided with an adsorption zone 1101, a cooling zone 1102, a desorption zone 1103 and a high temperature desorption zone 1104, and the second adsorption The runner 120 is provided with an adsorption zone 1201, a cooling zone 1202, a desorption zone 1203, and a high-temperature desorption zone 1204. Therefore, the present invention mainly lies in that the first adsorption runner 110 and the second adsorption runner 120 are provided with adsorption Zones 1101, 1201, cooling zones 1102, 1202 and desorption zones 1103, 1203 are also equipped with high-temperature desorption zones 1104, 1204, which can be used to turn on the remaining high-boiling organic substances during online operation (ON LINE) ( VOC) is released, so that the first adsorption runner 110 and the second adsorption runner 120 can restore their adsorption capacity, so that the first adsorption runner 110 and the second adsorption runner 120 can have four regions.

而該第一種實施方式的主要步驟(如第1圖所示)係包括：步驟S100輸入待吸附之氣體：該第一吸附轉輪110之吸附區1101的一側A係由一廢氣進氣管路111來輸入待吸附之氣體，而該第一吸附轉輪110之吸附區1101的另一側B則透過一第一淨氣排放管路112來輸送經過吸附後之氣體；透過該第一吸附轉輪110之吸附區1101的一側A係連接一廢氣進氣管路111(如第2圖及第3圖所示)，以 能由該廢氣進氣管路111來輸入待吸附之氣體，而該待吸附之氣體可以為揮發性有機化合物(VOC)、二氧化碳(CO2)、氮氣(N2)、水氣或氧氣(O2)之其中任一或複數組合之一，也可以是其他上述未表述之氣體，而該第一吸附轉輪110之吸附區1101的另一側B則與該一第一淨氣排放管路112之一端連接(如第2圖及第3圖所示)，讓該待吸附之氣體經該第一吸附轉輪110之吸附區1101進行吸附後再由該第一淨氣排放管路112來輸送經過吸附後之氣體。而完成上述步驟S100後即進行下一步驟S110。 The main steps of the first embodiment (as shown in FIG. 1) include: Step S100: Input gas to be adsorbed: Side A of the adsorption zone 1101 of the first adsorption runner 110 is fed by an exhaust gas The pipeline 111 is used to input the gas to be adsorbed, and the other side B of the adsorption area 1101 of the first adsorption runner 110 is used to convey the adsorbed gas through a first clean gas discharge line 112; One side A of the adsorption zone 1101 of the adsorption rotor 110 is connected to an exhaust gas intake line 111 (as shown in FIGS. 2 and 3) to The gas to be adsorbed can be input from the exhaust gas inlet line 111, and the gas to be adsorbed can be volatile organic compounds (VOC), carbon dioxide (CO2), nitrogen (N2), water vapor or oxygen (O2) Any one or one of the plural combinations may also be other gas not described above, and the other side B of the adsorption zone 1101 of the first adsorption runner 110 is connected to one end of the first clean gas discharge line 112 Connection (as shown in Figures 2 and 3), the gas to be adsorbed is adsorbed through the adsorption area 1101 of the first adsorption runner 110, and then is transported through the first clean gas discharge line 112 through the adsorption After the gas. After the above step S100 is completed, the next step S110 is performed.

另，下一步進行的步驟S110輸入用來冷卻之氣體：該第一吸附轉輪110之冷卻區1102的一側A係由一第一冷卻氣進氣管路113來輸入用來冷卻之氣體，而該第一吸附轉輪110之冷卻區1102的另一側B則透過一第一冷卻氣輸送管路114來連接至該第一加熱裝置130，以將經過該第一吸附轉輪110之冷卻區1102的氣體輸送到該第一加熱裝置130內；該第一吸附轉輪110之冷卻區1102的一側A係連接一第一冷卻氣進氣管路113(如第2圖及第3圖所示)，以供用來冷卻之氣體進入該第一吸附轉輪110之冷卻區1102來進行冷卻使用，而該第一吸附轉輪110之冷卻區1102的另一側B則連接一第一冷卻氣輸送管路114(如第2圖及第3圖所示)，該第一冷卻氣輸送管路114的另一端係與該第一加熱裝置130連接，使能將經過該第一吸附轉輪110之冷卻區1102的氣體輸送到該第一加熱裝置130內。 In addition, in the next step S110, the gas used for cooling is input: the side A of the cooling zone 1102 of the first adsorption runner 110 is supplied with a gas for cooling by a first cooling gas inlet line 113, The other side B of the cooling zone 1102 of the first adsorption runner 110 is connected to the first heating device 130 through a first cooling gas delivery pipe 114 to cool the first adsorption runner 110 The gas in zone 1102 is delivered to the first heating device 130; the side A of the cooling zone 1102 of the first adsorption runner 110 is connected to a first cooling gas inlet line 113 (as shown in FIGS. 2 and 3) (Shown), for the gas used for cooling to enter the cooling zone 1102 of the first adsorption runner 110 for cooling, and the other side B of the cooling zone 1102 of the first adsorption runner 110 is connected to a first cooling In the gas delivery line 114 (as shown in FIGS. 2 and 3), the other end of the first cooling gas delivery line 114 is connected to the first heating device 130 to enable the first suction runner to pass The gas in the cooling zone 1102 of 110 is delivered into the first heating device 130.

而上述該第一加熱裝置130係為加熱器、管道加熱器或熱 交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第一吸附轉輪110之冷卻區1102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪110之冷卻區1102的一側A所連接的第一冷卻氣進氣管路113乃是供新鮮空氣或外氣進入(如第2圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪110之冷卻區1102降溫用。另第二種實施態樣係該廢氣進氣管路111係設有一廢氣連通管路181，而該廢氣連通管路181的另一端係與該第一冷卻氣進氣管路113連接(如第3圖所示)，以能透過該廢氣連通管路181來將該廢氣進氣管路111內的廢氣輸送到該第一吸附轉輪110之冷卻區1102以進行降溫使用，另該廢氣連通管路181係設有一廢氣連通控制閥門1811(如第3圖所示)，以控制該廢氣連通管路181的風量。而完成上述步驟S110後即進行下一步驟S120。 The above-mentioned first heating device 130 is a heater, a pipe heater or a heat For any of the exchangers, the heater (not shown) is any of an electric heating wire, an electric heating tube, or an electric heating plate, and the pipe heater (not shown) is any of which uses gas fuel or liquid fuel One. In addition, the cooling zone 1102 of the first adsorption runner 110 described above is provided with two implementations, wherein the first implementation is the first connected to the side A of the cooling zone 1102 of the first adsorption runner 110 The cooling gas inlet line 113 is for fresh air or outside air to enter (as shown in FIG. 2 ), and provides cooling temperature of the cooling zone 1102 of the first adsorption runner 110 through the fresh air or outside air. Another second embodiment is that the exhaust gas intake line 111 is provided with an exhaust gas communication line 181, and the other end of the exhaust gas communication line 181 is connected to the first cooling gas intake line 113 (such as 3)), the exhaust gas in the exhaust gas inlet pipe 111 can be transmitted to the cooling zone 1102 of the first adsorption runner 110 through the exhaust gas communication pipe 181 for cooling, and the exhaust gas communication pipe The circuit 181 is provided with an exhaust gas communication control valve 1811 (as shown in FIG. 3) to control the air volume of the exhaust gas communication line 181. After the above step S110 is completed, the next step S120 is performed.

另，下一步進行的步驟S120輸送高溫熱氣進行脫附：該第一吸附轉輪110之脫附區1103的另一側B係由一第一熱氣輸送管路115來輸送該第一加熱裝置130內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路115係設有一第一熱氣旁通管路191，透過該第一熱氣旁通管路191連接至該第二加熱裝置140，而該第一吸附轉輪110之脫附區1103的一側A則透過一第一脫附濃縮氣體管路116來輸送經過脫附後之脫附濃縮氣體；該第一吸附轉輪110之脫附區1103的另一側B係與該一第一熱氣輸送管路115連接，且該第一熱氣輸送管路115的另一端則與該第一加熱裝置130連接(如第2圖及第 3圖所示)，以能將經由該第一加熱裝置130進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路115來輸送到該第一吸附轉輪110之脫附區1103來進行脫附使用。另該第一熱氣輸送管路115係設有一第一熱氣旁通管路191，該第一熱氣旁通管路191的另一端係與該第二加熱裝置140連接(如第2圖及第3圖所示)，以能將經由該第一加熱裝置130進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路191來輸送到該第二加熱裝置140內，另該第一吸附轉輪110之脫附區1103的一側A係連接一第一脫附濃縮氣體管路116的一端(如第2圖及第3圖所示)，以用輸送經過該第一吸附轉輪110之脫附區1103進行脫附後之脫附濃縮氣體。 In addition, the next step S120 is to transport high-temperature hot gas for desorption: the other side B of the desorption zone 1103 of the first adsorption runner 110 is transported by a first hot gas delivery pipeline 115 to the first heating device 130 The high-temperature hot gas generated therein is used for desorption, and the first hot gas delivery line 115 is provided with a first hot gas bypass line 191, which is connected to the second heating device 140 through the first hot gas bypass line 191 And the side A of the desorption zone 1103 of the first adsorption runner 110 conveys the desorbed concentrated gas after desorption through a first desorption concentrated gas line 116; the first adsorption runner 110 The other side B of the desorption zone 1103 is connected to the first hot gas delivery line 115, and the other end of the first hot gas delivery line 115 is connected to the first heating device 130 (as shown in FIGS. 2 and 3)), the high-temperature hot gas heated or exchanged by the first heating device 130 can be transported to the desorption zone 1103 of the first adsorption runner 110 through the first hot gas delivery pipeline 115 Use for desorption. In addition, the first hot gas delivery line 115 is provided with a first hot gas bypass line 191, and the other end of the first hot gas bypass line 191 is connected to the second heating device 140 (as shown in FIGS. 2 and 3) As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the first heating device 130 can be partially diverted and sent to the second heating device 140 through the first hot gas bypass line 191, and One side A of the desorption zone 1103 of the first adsorption runner 110 is connected to one end of a first desorption concentrated gas line 116 (as shown in FIGS. 2 and 3) for transportation through the first The desorption concentrated gas after the desorption zone 1103 of the adsorption rotor 110 performs desorption.

而上述該第二加熱裝置140係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該第一熱氣旁通管路191係設有一第一熱氣旁通控制閥門1911(如第3圖所示)，以控制該第一熱氣旁通管路191的風量，使能將經由該第一加熱裝置130進行加熱或熱交換的高溫熱氣部分分流到該第二加熱裝置140內。而完成上述步驟S120後即進行下一步驟S130。 The above-mentioned second heating device 140 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. And the first hot gas bypass line 191 is provided with a first hot gas bypass control valve 1911 (as shown in FIG. 3) to control the air volume of the first hot gas bypass line 191, so that The high-temperature hot gas that is heated or exchanged by the first heating device 130 is partially shunted into the second heating device 140. After the above step S120 is completed, the next step S130 is performed.

另，下一步進行的步驟S130再將高沸點有機物脫出：該第一吸附轉輪110之高溫脫附區1104的另一側B係由一第二熱氣輸送管路117來輸送由該第二加熱裝置140內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪110之高溫脫附 區1104的一側A則透過一第一高溫脫附濃縮氣體管路118來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路116內；該第一吸附轉輪110之高溫脫附區1104的另一側B係與一第二熱氣輸送管路117的一端連接，且該第二熱氣輸送管路117的另一端係與該第二加熱裝置140連接(如第2圖及第3圖所示)，透過該第二加熱裝置140來將進入該第二熱氣輸送管路117內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路117內的高溫熱氣再輸送到該第一吸附轉輪110之高溫脫附區1104，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪110能恢復其吸附能力，另該第一吸附轉輪110之高溫脫附區1104的一側A係連接一第一高溫脫附濃縮氣體管路118(如第2圖及第3圖所示)，而該第一高溫脫附濃縮氣體管路118的另一端係與該第一脫附濃縮氣體管路116連接，以將經過該第一吸附轉輪110之高溫脫附區1104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路118來輸送到該第一脫附濃縮氣體管路116內。 In addition, the next step S130 is to remove the high-boiling organic matter: the other side B of the high-temperature desorption zone 1104 of the first adsorption runner 110 is conveyed by a second hot gas conveying line 117 by the second The high-temperature hot gas raised to a certain temperature in the heating device 140 to remove high-boiling organics (VOC), and the high-temperature desorption of the first adsorption runner 110 The side A of the zone 1104 transfers the high-temperature desorption concentrated gas after desorption to the first desorption concentrated gas line 116 through a first high-temperature desorption concentrated gas line 118; the first adsorption runner The other side B of the high-temperature desorption zone 1104 of 110 is connected to one end of a second hot gas delivery line 117, and the other end of the second hot gas delivery line 117 is connected to the second heating device 140 (e.g. 2 and 3), through the second heating device 140 to raise the high temperature hot gas entering the second hot gas delivery pipe 117 to a certain temperature (for example, 300 ℃), and the second hot gas delivery pipe The high-temperature hot gas in the path 117 is sent to the high-temperature desorption zone 1104 of the first adsorption runner 110 for high-temperature desorption. When online operation (ON LINE), the remaining high-boiling organic matter (VOC) ) Is released, so that the first adsorption runner 110 can restore its adsorption capacity, and the side A of the high temperature desorption zone 1104 of the first adsorption runner 110 is connected to a first high temperature desorption concentrated gas line 118 ( (As shown in FIGS. 2 and 3), and the other end of the first high-temperature desorption concentrated gas line 118 is connected to the first desorption concentrated gas line 116 to pass the first adsorption runner The high-temperature desorption concentrated gas desorbed by the high-temperature desorption zone 1104 of 110 can be transported into the first desorption concentrated gas line 116 through the first high-temperature desorption concentrated gas line 118.

而上述該第一脫附濃縮氣體管路116的另一端係與一焚燒裝置100連接(如第2圖及第3圖所示)，其中該焚燒裝置100係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第一種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置100乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置100不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置100為蓄熱式焚燒爐 (RTO)時，該蓄熱式焚燒爐(RTO)係設有入口101及出口102，而該入口101係與該第一脫附濃縮氣體管路116連接，其中該第一脫附濃縮氣體管路116另有與該第一高溫脫附濃縮氣體管路118的另一端連接，以將經過該第一吸附轉輪110之高溫脫附區1104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路118來輸送到該第一脫附濃縮氣體管路116內，使該第一脫附濃縮氣體管路116內除了經過該第一吸附轉輪110之脫附區1103所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路116內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口102則連接至一煙囪170(如第2圖及第3圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪170來排出，另該第一脫附濃縮氣體管路116係設有一風機1161(如第3圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口101內，讓脫附濃縮氣體能進行高溫裂解。而完成上述步驟S130後即進行下一步驟S140。 The other end of the first desorption concentrated gas line 116 is connected to an incinerator 100 (as shown in FIGS. 2 and 3), wherein the incinerator 100 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown) or regenerative incinerator (RTO), and the illustration of the first embodiment of the present invention takes the regenerative incinerator (RTO) as an example, Moreover, the incinerator 100 described below is a regenerative incinerator (RTO), but the incinerator 100 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (FIG. Not shown) or catalyst furnace (not shown). When the incinerator 100 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 101 and an outlet 102, and the inlet 101 is connected to the first desorption concentrated gas line 116, wherein the first desorption concentrated gas line 116 is additionally connected to the other end of the first high-temperature desorption concentrated gas line 118 to pass the high-temperature desorption concentrated gas desorbed through the high-temperature desorption zone 1104 of the first adsorption runner 110 through the first A high-temperature desorption concentrated gas line 118 is delivered to the first desorption concentrated gas line 116, so that the first desorption concentrated gas line 116 passes through the desorption zone 1103 of the first adsorption runner 110 The desorbed concentrated gas also contains high-temperature desorbed concentrated gas, so that the high-temperature desorbed concentrated gas can enter the regenerative incinerator together with the desorbed concentrated gas in the first desorbed concentrated gas line 116 ( RTO) high-temperature cracking to reduce volatile organic compounds, and the outlet 102 of the regenerative incinerator (RTO) is connected to a chimney 170 (as shown in Figures 2 and 3) to pass the high temperature The clean gas after cracking the organic compound can be discharged by the chimney 170, and the first desorption concentrated gas line 116 is provided with a fan 1161 (as shown in FIG. 3) to push and pull the desorption concentrated gas into The inlet 101 of the regenerative incinerator (RTO) allows the desorbed concentrated gas to undergo high-temperature cracking. After the above step S130 is completed, the next step S140 is performed.

另，下一步進行的步驟S140輸送欲再吸附之氣體：該第二吸附轉輪120之吸附區1201的一側A係由該第一淨氣排放管路112來輸送欲進行再吸附之氣體，而該第二吸附轉輪120之吸附區1201的另一側B則透過一第二淨氣排放管路121來輸送經過再吸附後之氣體；該第二吸附轉輪120之吸附區1201的一側A係與該第一淨氣排放管路112的另一端相連接(如第2圖及第3圖所示)，使該第一淨氣排放管路112內經過吸附後之氣體能直接再輸送到該第二吸附轉輪12 0之吸附區1201內進行再吸附，另該第二吸附轉輪120之吸附區1201的另一側B係連接一第二淨氣排放管路121，並透過該第二淨氣排放管路121來輸送經過再吸附後之氣體。 In addition, the next step S140 is to transport the gas to be re-adsorbed: the side A of the adsorption area 1201 of the second adsorption rotor 120 is to transport the gas to be re-adsorbed by the first clean gas discharge line 112, The other side B of the adsorption zone 1201 of the second adsorption runner 120 conveys the re-adsorbed gas through a second clean gas discharge line 121; one of the adsorption zones 1201 of the second adsorption runner 120 Side A is connected to the other end of the first clean gas discharge line 112 (as shown in FIGS. 2 and 3), so that the adsorbed gas in the first clean gas discharge line 112 can be directly recycled Conveyed to the second suction runner 12 The re-adsorption is performed in the adsorption zone 1201 of 0, and the other side B of the adsorption zone 1201 of the second adsorption runner 120 is connected to a second clean gas discharge line 121 and passes through the second clean gas discharge line 121 To transport the gas after re-adsorption.

而上述該第二淨氣排放管路121之另一端則與一煙囪170連接(如第2圖及第3圖所示)，以方便將經由該第一吸附轉輪110之吸附區1101及該第二吸附轉輪120之吸附區1201所吸附過後之氣體透過該煙囪170來進行排放，其中該第二淨氣排放管路121係設有一風機1211(如第3圖所示)，以增加氣體之流速來流向該煙囪170。而完成上述步驟S140後即進行下一步驟S150。 The other end of the second clean gas discharge line 121 is connected to a chimney 170 (as shown in FIGS. 2 and 3) to facilitate the adsorption area 1101 passing through the first adsorption runner 110 and the The gas adsorbed by the adsorption area 1201 of the second adsorption runner 120 is discharged through the chimney 170, wherein the second clean gas discharge line 121 is provided with a fan 1211 (as shown in FIG. 3) to increase the gas The flow velocity comes to the chimney 170. After the above step S140 is completed, the next step S150 is performed.

另，下一步進行的步驟S150輸入用來冷卻之氣體：該第二吸附轉輪120之冷卻區1202的一側A係由一第二冷卻氣進氣管路122來輸入用來冷卻之氣體，而該第二吸附轉輪120之冷卻區1202的另一側B則透過一第二冷卻氣輸送管路123來連接至該第三加熱裝置150，以將經過該第二吸附轉輪120之冷卻區1202的氣體輸送到該第三加熱裝置150內；該第二吸附轉輪120之冷卻區1202的一側A係連接一第二冷卻氣進氣管路122(如第2圖及第3圖所示)，以供用來冷卻之氣體進入該第二吸附轉輪120之冷卻區1202來進行冷卻使用，而該第二吸附轉輪120之冷卻區1202的另一側B則連接一第二冷卻氣輸送管路123(如第2圖及第3圖所示)，該第二冷卻氣輸送管路123的另一端係與該第三加熱裝置150連接，使能將經過該第二吸附轉輪120之冷卻區1202的氣體輸送到該第三加熱裝置150內。 In addition, in the next step S150, the gas used for cooling is input: the side A of the cooling area 1202 of the second adsorption runner 120 is supplied with a gas for cooling by a second cooling gas inlet line 122, The other side B of the cooling zone 1202 of the second adsorption runner 120 is connected to the third heating device 150 through a second cooling gas delivery line 123 to cool the passing of the second adsorption runner 120 The gas in the area 1202 is delivered to the third heating device 150; the side A of the cooling area 1202 of the second adsorption runner 120 is connected to a second cooling gas inlet line 122 (as shown in FIGS. 2 and 3) (Shown), for the gas used for cooling to enter the cooling zone 1202 of the second adsorption runner 120 for cooling, and the other side B of the cooling zone 1202 of the second adsorption runner 120 is connected to a second cooling The gas conveying pipeline 123 (as shown in FIGS. 2 and 3), the other end of the second cooling gas conveying pipeline 123 is connected to the third heating device 150, enabling the second adsorption runner to pass The gas in the cooling zone 1202 of 120 is delivered to the third heating device 150.

而上述該第三加熱裝置150係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第二吸附轉輪120之冷卻區1202係設有兩種實施態樣，其中第一種實施態樣為該第二吸附轉輪之120冷卻區1202的一側A所連接的第二冷卻氣進氣管路122乃是供新鮮空氣或外氣進入(如第2圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪120之冷卻區1202降溫用。另第二種實施態樣係該第一淨氣排放管路112係設有一第一淨氣連通管路182，而該第一淨氣連通管路182的另一端係與該第二冷卻氣進氣管路122連接(如第3圖所示)，以能透過該第一淨氣連通管路182來將該第一淨氣排放管路112內的氣體輸送到該第二吸附轉輪120之冷卻區1202以進行降溫使用，另該第一淨氣連通管路182係設有一第一淨氣連通控制閥門1821(如第3圖所示)，以控制該第一淨氣連通管路182的風量。而完成上述步驟S150後即進行下一步驟S160。 The above-mentioned third heating device 150 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling area 1202 of the second adsorption runner 120 is provided with two implementations, wherein the first implementation is the second side A connected to the side A of the cooling zone 1202 of the second adsorption runner 120 The cooling gas inlet line 122 is for fresh air or outside air to enter (as shown in FIG. 2 ), and the cooling area 1202 of the second adsorption runner 120 is provided for cooling through the fresh air or outside air. In another second embodiment, the first clean gas discharge line 112 is provided with a first clean gas communication line 182, and the other end of the first clean gas communication line 182 is connected to the second cooling gas The gas line 122 is connected (as shown in FIG. 3) so that the gas in the first clean gas discharge line 112 can be sent to the second adsorption runner 120 through the first clean gas communication line 182 The cooling zone 1202 is used for cooling. In addition, the first clean air communication line 182 is provided with a first clean air communication control valve 1821 (as shown in FIG. 3) to control the first clean air communication line 182 Air volume. After the above step S150 is completed, the next step S160 is performed.

另，下一步進行的步驟S160輸送高溫熱氣進行脫附：該第二吸附轉輪120之脫附區1203的另一側B係由一第三熱氣輸送管路124來輸送該第三加熱裝置150內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路124係設有一第三熱氣旁通管路192，透過該第三熱氣旁通管路192連接至該第四加熱裝置160，而該第二吸附轉輪120之脫附區1203的一側A則透過一第二脫附濃縮氣體管路125來輸送經過脫附後之脫附濃縮氣體；該第二吸附轉輪120之脫附區1 203的另一側B係與該一第三熱氣輸送管路124連接，且該第三熱氣輸送管路124的另一端則與該第三加熱裝置150連接(如第2圖及第3圖所示)，以能將經由該第三加熱裝置150進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路124來輸送到該第二吸附轉輪120之脫附區1203來進行脫附使用。另該第三熱氣輸送管路124係設有一第三熱氣旁通管路192(如第2圖及第3圖所示)，該第三熱氣旁通管路192的另一端係與該第四加熱裝置160連接，以能將經由該第三加熱裝置150進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路192來輸送到該第四加熱裝置160內，另該第二吸附轉輪120之脫附區1203的一側A係連接一第二脫附濃縮氣體管路125的一端(如第2圖及第3圖所示)，以用輸送經過該第二吸附轉輪120之脫附區1203進行脫附後之脫附濃縮氣體。 In addition, the next step S160 is to transport high-temperature hot gas for desorption: the other side B of the desorption zone 1203 of the second adsorption runner 120 is transported by a third hot gas delivery pipeline 124 to the third heating device 150 The high-temperature hot gas generated therein is used for desorption, and the third hot gas delivery pipe 124 is provided with a third hot gas bypass pipe 192, which is connected to the fourth heating device 160 through the third hot gas bypass pipe 192 , And the side A of the desorption area 1203 of the second adsorption runner 120 conveys the desorbed concentrated gas after desorption through a second desorption concentrated gas line 125; the second adsorption runner 120 Desorption Zone 1 The other side B of 203 is connected to the third hot gas delivery pipe 124, and the other end of the third hot gas delivery pipe 124 is connected to the third heating device 150 (as shown in FIGS. 2 and 3) (Show)), the high-temperature hot gas heated or exchanged by the third heating device 150 can be transported to the desorption area 1203 of the second adsorption runner 120 through the third hot gas delivery pipe 124 for desorption . In addition, the third hot gas delivery pipeline 124 is provided with a third hot gas bypass pipeline 192 (as shown in FIGS. 2 and 3 ). The other end of the third hot gas bypass pipeline 192 is connected to the fourth The heating device 160 is connected so that the high-temperature hot gas that is heated or exchanged through the third heating device 150 can be partially shunted, and is transferred to the fourth heating device 160 through the third hot gas bypass line 192, and One side A of the desorption zone 1203 of the second adsorption runner 120 is connected to one end of a second desorption concentrated gas line 125 (as shown in FIGS. 2 and 3) for transportation through the second The desorption concentrated gas after the desorption zone 1203 of the adsorption rotor 120 performs desorption.

而上述該第四加熱裝置160係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該第三熱氣旁通管路192係設有一第三熱氣旁通控制閥門1921(如第3圖所示)，以控制該第三熱氣旁通管路192的風量，使能將經由該第三加熱裝置150進行加熱或熱交換的高溫熱氣部分分流到該第四加熱裝置160內。而完成上述步驟S160後即進行下一步驟S170。 The above-mentioned fourth heating device 160 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. And the third hot gas bypass line 192 is provided with a third hot gas bypass control valve 1921 (as shown in FIG. 3) to control the air volume of the third hot gas bypass line 192, so that the The high-temperature hot gas that is heated or exchanged by the third heating device 150 is partially shunted into the fourth heating device 160. After the above step S160 is completed, the next step S170 is performed.

另，下一步進行的步驟S170再將高沸點有機物脫出：該第二吸附轉輪120之高溫脫附區1204的另一側B係由一第四熱氣輸 送管路126來輸送由該第四加熱裝置160內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪120之高溫脫附區1204的一側A則透過一第二高溫脫附濃縮氣體管路127來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路125內；該第二吸附轉輪120之高溫脫附區1204的另一側B係與一第四熱氣輸送管路126的一端連接，且該第四熱氣輸送管路126的另一端係與該第四加熱裝置160連接(如第2圖及第3圖所示)，透過該第四加熱裝置160來將進入該第四熱氣輸送管路126內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路126內的高溫熱氣再輸送到該第二吸附轉輪120之高溫脫附區1204，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪120能恢復其吸附能力，另該第二吸附轉輪120之高溫脫附區1204的一側A係連接一第二高溫脫附濃縮氣體管路127(如第2圖及第3圖所示)，而該第二高溫脫附濃縮氣體管路127的另一端係與該第二脫附濃縮氣體管路125連接，以將經過該第二吸附轉輪120之高溫脫附區1204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路127來輸送到該第二脫附濃縮氣體管路125內。 In addition, in the next step S170, high-boiling organics are removed: the other side B of the high-temperature desorption zone 1204 of the second adsorption runner 120 is transported by a fourth hot gas The pipeline 126 is used to transport high-temperature hot gas raised to a certain temperature by the fourth heating device 160 to remove high-boiling organic compounds (VOC), and a high-temperature desorption zone 1204 of the second adsorption runner 120 Side A sends a high-temperature desorption concentrated gas after desorption through a second high-temperature desorption concentrated gas line 127 to the second desorption concentrated gas line 125; the high-temperature desorption of the second adsorption runner 120 The other side B of the attached area 1204 is connected to one end of a fourth hot gas delivery line 126, and the other end of the fourth hot gas delivery line 126 is connected to the fourth heating device 160 (as shown in FIGS. 2 and 3)), through the fourth heating device 160, the high-temperature hot gas entering the fourth hot gas delivery pipe 126 can be raised to a certain temperature (for example, 300 ℃), and the fourth hot gas delivery pipe 126 The high-temperature hot gas is transported to the high-temperature desorption zone 1204 of the second adsorption runner 120 for high-temperature desorption. When online operation (ON LINE), the remaining high-boiling organic matter (VOC) can be removed. The second adsorption runner 120 can restore its adsorption capacity, and the side A of the high temperature desorption zone 1204 of the second adsorption runner 120 is connected to a second high temperature desorption concentrated gas line 127 (as shown in FIG. 2 And Figure 3), and the other end of the second high-temperature desorption concentrated gas line 127 is connected to the second desorption concentrated gas line 125 to decouple the high temperature passing through the second adsorption runner 120 The high-temperature desorption concentrated gas desorbed in the attachment zone 1204 can be transported into the second desorption concentrated gas line 125 through the second high-temperature desorption concentrated gas line 127.

而上述該第二脫附濃縮氣體管路125的另一端係與一焚燒裝置100連接(如第2圖及第3圖所示)，其中該焚燒裝置100係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第一種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置100乃是為蓄熱式焚燒爐(RTO)，但本發明的 焚燒裝置100不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置100為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口101及出口102，而該入口101係與該第二脫附濃縮氣體管路125連接，其中該第二脫附濃縮氣體管路125另有與該第二高溫脫附濃縮氣體管路127的另一端連接，以將經過該第二吸附轉輪120之高溫脫附區1204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路127來輸送到該第二脫附濃縮氣體管路125內，使該第二脫附濃縮氣體管路125內除了經過該第二吸附轉輪120之脫附區1203所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路125內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口102則連接至一煙囪170(如第2圖及第3圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪170來排出，另該第二脫附濃縮氣體管路125係設有一風機1251(如第3圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口101內，讓脫附濃縮氣體能進行高溫裂解。 The other end of the second desorbed concentrated gas pipeline 125 is connected to an incinerator 100 (as shown in FIGS. 2 and 3), wherein the incinerator 100 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown) or regenerative incinerator (RTO), and the illustration of the first embodiment of the present invention takes the regenerative incinerator (RTO) as an example, And the incinerator 100 described below is a regenerative incinerator (RTO), but the present invention The incinerator 100 is not limited to a regenerative incinerator (RTO), but may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 100 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 101 and an outlet 102, and the inlet 101 is connected to the second desorption concentrated gas pipeline 125 , Wherein the second desorption concentrated gas pipeline 125 is additionally connected to the other end of the second high-temperature desorption concentrated gas pipeline 127 to desorb the high-temperature desorption zone 1204 passing through the second adsorption runner 120 The lower high-temperature desorption concentrated gas can be transported into the second desorption concentrated gas line 125 through the second high-temperature desorption concentrated gas line 127, so that the second desorption concentrated gas line 125 passes through the The desorption concentrated gas desorbed by the desorption zone 1203 of the second adsorption runner 120 also contains high-temperature desorption concentrated gas, so that the high-temperature desorption concentrated gas can be desorbed from the second desorption concentrated gas pipeline 125 The concentrated gas enters the regenerative incinerator (RTO) for high-temperature cracking to reduce volatile organic compounds, and the outlet 102 of the regenerative incinerator (RTO) is connected to a chimney 170 (as shown in Figure 2 and (Shown in Figure 3), so that the clean gas after pyrolysis of organic compounds can be discharged through the chimney 170, and the second desorption concentrated gas pipeline 125 is provided with a fan 1251 (as shown in Figure 3) In order to push the desorbed concentrated gas into the inlet 101 of the regenerative incinerator (RTO), the desorbed concentrated gas can be pyrolyzed at high temperature.

而本發明第一種實施架構的具高溫脫附之轉輪系統(如第2圖及第3圖所示)，主要係透過一第一吸附轉輪110、一第二吸附轉輪120、一第一加熱裝置130、一第二加熱裝置140、一第三加熱裝置150及一第四加熱裝置160之組合設計，而本發明第一種實施架構的第一吸附轉輪110係設有吸附區1101、冷卻區1102、脫附區1 103及高溫脫附區1104，該第一吸附轉輪110係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且一廢氣進氣管路111係連接至該第一吸附轉輪110之吸附區1101的一側A(如第2圖及第3圖所示)，以使該第一吸附轉輪110之吸附區1101能吸附該廢氣進氣管路111內的有機物，而該第一吸附轉輪110之吸附區1101的另一側B係與該一第一淨氣排放管路112之一端連接，讓該廢氣經該第一吸附轉輪110之吸附區1101進行吸附有機物後再由該第一淨氣排放管路112來輸送。 The first embodiment of the present invention is a high-temperature desorption rotor system (as shown in Figure 2 and Figure 3), mainly through a first adsorption runner 110, a second adsorption runner 120, a The combined design of the first heating device 130, a second heating device 140, a third heating device 150 and a fourth heating device 160, and the first adsorption rotor 110 of the first embodiment of the present invention is provided with an adsorption zone 1101, cooling zone 1102, desorption zone 1 103 and a high temperature desorption zone 1104, the first adsorption runner 110 is a zeolite concentration runner or a concentration runner of other materials, and an exhaust gas intake line 111 is connected to the adsorption of the first adsorption runner 110 One side A of the area 1101 (as shown in FIGS. 2 and 3), so that the adsorption area 1101 of the first adsorption runner 110 can adsorb organic matter in the exhaust gas intake line 111, and the first adsorption The other side B of the adsorption zone 1101 of the runner 110 is connected to one end of the first clean gas discharge line 112 to allow the exhaust gas to adsorb organic matter through the adsorption zone 1101 of the first adsorption runner 110 before being discharged by the The first clean gas discharge line 112 is used for transportation.

另該第一吸附轉輪110之冷卻區1102的一側A係連接一第一冷卻氣進氣管路113(如第2圖及第3圖所示)，以供氣體進入該第一吸附轉輪110之冷卻區1102來進行冷卻使用，而該第一吸附轉輪110之冷卻區1102的另一側B係連接一第一冷卻氣輸送管路114(如第2圖及第3圖所示)，該第一冷卻氣輸送管路114的另一端係與該第一加熱裝置130連接，其中該第一加熱裝置130係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第一熱氣輸送管路115的一端係與該第一吸附轉輪110之脫附區1103的另一側B連接(如第2圖及第3圖所示)，且該第一熱氣輸送管路115的另一端則與該第一加熱裝置130連接，以能將經由該第一加熱裝置130進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路115來輸送到該第一吸附轉輪110之脫附區1103來進行脫附使用。 In addition, one side A of the cooling zone 1102 of the first adsorption runner 110 is connected to a first cooling gas inlet line 113 (as shown in FIGS. 2 and 3) for gas to enter the first adsorption rotor The cooling zone 1102 of the wheel 110 is used for cooling, and the other side B of the cooling zone 1102 of the first adsorption runner 110 is connected to a first cooling gas delivery line 114 (as shown in FIGS. 2 and 3) ), the other end of the first cooling gas delivery pipe 114 is connected to the first heating device 130, wherein the first heating device 130 is any one of a heater, a pipe heater or a heat exchanger, the heating The heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the duct heater (not shown) is any one of using gas fuel or liquid fuel. One end of the first hot gas delivery line 115 is connected to the other side B of the desorption zone 1103 of the first adsorption runner 110 (as shown in FIGS. 2 and 3), and the first hot gas The other end of the conveying pipe 115 is connected to the first heating device 130 so that high-temperature hot gas heated or exchanged through the first heating device 130 can be conveyed to the first through the first hot gas conveying line 115 The desorption area 1103 of the adsorption rotor 110 is used for desorption.

而上述該第一吸附轉輪110之冷卻區1102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪110之冷卻區1102的一側A所連接的第一冷卻氣進氣管路113乃是供新鮮空氣或外氣進入(如第2圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪110之冷卻區1102降溫用。另第二種實施態樣係該廢氣進氣管路111係設有一廢氣連通管路181，而該廢氣連通管路181的另一端係與該第一冷卻氣進氣管路113連接(如第3圖所示)，以能透過該廢氣連通管路181來將該廢氣進氣管路111內的廢氣輸送到該第一吸附轉輪110之冷卻區1102以進行降溫使用，另該廢氣連通管路181係設有一廢氣連通控制閥門1811(如第3圖所示)，以控制該廢氣連通管路181的風量。 The cooling zone 1102 of the first adsorption runner 110 is provided with two implementations, wherein the first implementation is the first side A connected to the side A of the cooling zone 1102 of the first adsorption runner 110 The cooling gas inlet line 113 is for fresh air or outside air to enter (as shown in FIG. 2 ), and provides cooling temperature of the cooling zone 1102 of the first adsorption runner 110 through the fresh air or outside air. Another second embodiment is that the exhaust gas intake line 111 is provided with an exhaust gas communication line 181, and the other end of the exhaust gas communication line 181 is connected to the first cooling gas intake line 113 (such as 3)), the exhaust gas in the exhaust gas inlet pipe 111 can be transmitted to the cooling zone 1102 of the first adsorption runner 110 through the exhaust gas communication pipe 181 for cooling, and the exhaust gas communication pipe The circuit 181 is provided with an exhaust gas communication control valve 1811 (as shown in FIG. 3) to control the air volume of the exhaust gas communication line 181.

另該一第一脫附濃縮氣體管路116的一端係與該第一吸附轉輪110之脫附區1103的一側A連接，而該第一脫附濃縮氣體管路116的另一端係與一焚燒裝置100連接(如第2圖及第3圖所示)，其中該焚燒裝置100係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第一種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置100乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置100不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置100為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口101及出口102，而該入口101係與該第一脫附濃縮氣體管路116連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第一脫附濃縮氣體管路116 來輸送到該蓄熱式焚燒爐(RTO)之入口101，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口102則連接至一煙囪170(如第2圖及第3圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪170來排出，另該第一脫附濃縮氣體管路116係設有一風機1161，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口101內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the first desorption concentrated gas line 116 is connected to one side A of the desorption zone 1103 of the first adsorption runner 110, and the other end of the first desorption concentrated gas line 116 is connected to An incineration device 100 is connected (as shown in Figures 2 and 3), wherein the incineration device 100 is a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative type One of the incinerators (RTO), and the illustration of the first implementation structure of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 100 described below is a regenerative incinerator (RTO) However, the incinerator 100 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 100 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 101 and an outlet 102, and the inlet 101 is connected to the first desorption concentrated gas line 116 , So that the desorbed concentrated gas desorbed by high temperature can pass through the first desorbed concentrated gas line 116 To the inlet 101 of the regenerative incinerator (RTO), so that the desorbed concentrated gas can enter the regenerative incinerator (RTO) for high-temperature cracking to reduce volatile organic compounds, and the regenerative incinerator ( RTO) outlet 102 is connected to a chimney 170 (as shown in Figures 2 and 3), so that the clean gas after high-temperature cracking of organic matter can be discharged from the chimney 170, and the first desorption concentrated gas The pipeline 116 is provided with a fan 1161 to push and pull the desorbed concentrated gas into the inlet 101 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to undergo high-temperature cracking.

而本發明第一種實施架構(如第2圖及第3圖所示)中主要在於該第一吸附轉輪110除了設有吸附區1101、冷卻區1102及脫附區1103外，還設有高溫脫附區1104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪110能恢復其吸附能力，使該第一吸附轉輪110能具有四個區域。而該第一吸附轉輪110之高溫脫附區1104的另一側B係與一第二熱氣輸送管路117的一端連接，且該第二熱氣輸送管路117的另一端係與該第二加熱裝置140連接(如第2圖及第3圖所示)，其中該第二加熱裝置140係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第一熱氣輸送管路115係設有一第一熱氣旁通管路191，該第一熱氣旁通管路191的另一端係與該第二加熱裝置140連接(如第2圖及第3圖所示)，以能將經由該第一加熱裝置130進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路191來輸送到該第二加熱裝置140內，以將進入 該第二熱氣輸送管路117內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路117內的高溫熱氣再輸送到該第一吸附轉輪110之高溫脫附區1104，以供進行高溫脫附使用，另該第一熱氣旁通管路191係設有一第一熱氣旁通控制閥門1911(如第3圖所示)，以控制該第一熱氣旁通管路191的風量。 The first implementation structure of the present invention (as shown in FIG. 2 and FIG. 3) mainly lies in that the first adsorption rotor 110 is provided with an adsorption zone 1101, a cooling zone 1102 and a desorption zone 1103. The high-temperature desorption zone 1104 can be used to remove the remaining high-boiling organic compounds (VOC) during online operation (ON LINE), so that the first adsorption runner 110 can restore its adsorption capacity, so that the first adsorption The runner 110 can have four areas. The other side B of the high-temperature desorption zone 1104 of the first adsorption runner 110 is connected to one end of a second hot gas delivery pipe 117, and the other end of the second hot gas delivery pipe 117 is connected to the second The heating device 140 is connected (as shown in Figures 2 and 3), wherein the second heating device 140 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is It is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown in the figure) is any one using gas fuel or liquid fuel. The first hot gas delivery line 115 is provided with a first hot gas bypass line 191, and the other end of the first hot gas bypass line 191 is connected to the second heating device 140 (as shown in FIGS. 2 and 3) As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the first heating device 130 can be partially diverted and sent to the second heating device 140 through the first hot gas bypass line 191 to Will enter The high-temperature hot gas in the second hot gas delivery line 117 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the second hot gas delivery line 117 is sent to the high-temperature desorption of the first adsorption runner 110 Zone 1104 for high temperature desorption, and the first hot gas bypass line 191 is provided with a first hot gas bypass control valve 1911 (as shown in FIG. 3) to control the first hot gas bypass pipe The air volume of Road 191.

再者，該第一吸附轉輪110之高溫脫附區1104的一側A係連接一第一高溫脫附濃縮氣體管路118(如第2圖及第3圖所示)，而該第一高溫脫附濃縮氣體管路118的另一端係與該第一脫附濃縮氣體管路116連接，以將經過該第一吸附轉輪110之高溫脫附區1104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路118來輸送到該第一脫附濃縮氣體管路116內，再透過該第一脫附濃縮氣體管路116輸送到該蓄熱式焚燒爐(RTO)之入口101，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路116內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, a side A of the high-temperature desorption zone 1104 of the first adsorption runner 110 is connected to a first high-temperature desorption concentrated gas line 118 (as shown in FIGS. 2 and 3), and the first The other end of the high-temperature desorption concentrated gas line 118 is connected to the first desorption concentrated gas line 116 to condense the high-temperature desorption concentrated through the high-temperature desorption zone 1104 of the first adsorption runner 110 Gas can be transported into the first desorption concentrated gas line 116 through the first high-temperature desorption concentrated gas line 118, and then transferred to the regenerative incinerator (RTO) through the first desorption concentrated gas line 116 ) Of the inlet 101, allowing the high-temperature desorption concentrated gas to enter the regenerative incinerator (RTO) together with the desorption concentrated gas in the first desorption concentrated gas line 116 for high-temperature cracking.

另該第二吸附轉輪120係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且該第二吸附轉輪120內係設有吸附區1201、冷卻區1202、脫附區1203及高溫脫附區1204，而該第二吸附轉輪120之吸附區1201的一側A係與該第一淨氣排放管路112的另一端相連接(如第2圖及第3圖所示)，使該第一淨氣排放管路112內的氣體能直接再輸送到該第二吸附轉輪120之吸附區1201內進行吸附，另該第二吸附轉輪120之吸附區1201的另一側B係連接一第二淨氣排放管路121，而該第二淨氣排放管路121之另一端則與一煙囪170 連接(如第2圖及第3圖所示)，以方便將經由該第一吸附轉輪110之吸附區1101及該第二吸附轉輪120之吸附區1201所吸附過的氣體透過該煙囪170來進行排放，其中該第二淨氣排放管路121係設有一風機1211(如第3圖所示)，以增加氣體之流速來流向該煙囪170。 In addition, the second adsorption runner 120 is a zeolite concentration runner or a concentration runner of other materials, and the second adsorption runner 120 is provided with an adsorption zone 1201, a cooling zone 1202, a desorption zone 1203, and a high temperature desorption Attached area 1204, and one side A of the adsorption area 1201 of the second adsorption rotor 120 is connected to the other end of the first clean gas discharge line 112 (as shown in FIGS. 2 and 3), so that The gas in the first clean gas discharge line 112 can be directly sent to the adsorption area 1201 of the second adsorption rotor 120 for adsorption, and the other side of the adsorption area 1201 of the second adsorption rotor 120 is B A second clean gas discharge line 121 is connected, and the other end of the second clean gas discharge line 121 is connected to a chimney 170 Connection (as shown in Figures 2 and 3) to facilitate the passage of gas adsorbed through the adsorption zone 1101 of the first adsorption runner 110 and the adsorption zone 1201 of the second adsorption runner 120 through the chimney 170 To discharge, the second clean gas discharge line 121 is provided with a fan 1211 (as shown in FIG. 3) to increase the flow velocity of the gas to the chimney 170.

另該第二吸附轉輪120之冷卻區1202的一側A係連接一第二冷卻氣進氣管路122，以供氣體進入該第二吸附轉輪120之冷卻區1202來進行冷卻使用，而該第二吸附轉輪120之冷卻區1202的另一側B係連接一第二冷卻氣輸送管路123(如第2圖及第3圖所示)，該第二冷卻氣輸送管路123的另一端係與該第三加熱裝置150連接，其中該第三加熱裝置150係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第三熱氣輸送管路124的一端係與該第二吸附轉輪120之脫附區1203的另一側B連接，且該第三熱氣輸送管路124的另一端係與該第三加熱裝置150連接(如第2圖及第3圖所示)，以能將經由該第三加熱裝置150進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路124來輸送到該第二吸附轉輪120之脫附區1203來進行脫附使用。 In addition, one side A of the cooling zone 1202 of the second adsorption runner 120 is connected to a second cooling gas inlet line 122 for the gas to enter the cooling zone 1202 of the second adsorption runner 120 for cooling, and The other side B of the cooling zone 1202 of the second adsorption runner 120 is connected to a second cooling gas delivery line 123 (as shown in FIGS. 2 and 3). The other end is connected to the third heating device 150, wherein the third heating device 150 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is an electric heating wire or an electric heater Either a tube or an electric heating plate, the pipe heater (not shown) is either gas fuel or liquid fuel. One end of the third hot gas delivery pipe 124 is connected to the other side B of the desorption zone 1203 of the second adsorption runner 120, and the other end of the third hot gas delivery pipe 124 is connected to the third The heating device 150 is connected (as shown in FIGS. 2 and 3) so that high-temperature hot gas heated or exchanged through the third heating device 150 can be transported to the second through the third hot gas delivery line 124 The desorption area 1203 of the adsorption rotor 120 is used for desorption.

而上述該第二吸附轉輪120之冷卻區1202係設有兩種實施態樣，其中第一種實施態樣為該第二吸附轉輪120之冷卻區1202的一側A所連接的第二冷卻氣進氣管路122乃是供新鮮空氣或外氣進入(如第2圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪120之冷卻區1202降溫用。另第二種實施態樣係該第一淨氣排放管路1 12係設有一第一淨氣連通管路182，而該第一淨氣連通管路182的另一端係與該第二冷卻氣進氣管路122連接(如第3圖所示)，以能透過該第一淨氣連通管路182來將該第一淨氣排放管路112內的氣體輸送到該第二吸附轉輪120之冷卻區1202以進行降溫使用，另該第一淨氣連通管路182係設有一第一淨氣連通控制閥門1821(如第3圖所示)，以控制該第一淨氣連通管路182的風量。 The cooling zone 1202 of the second adsorption runner 120 is provided with two implementations, wherein the first implementation is the second side A connected to the side A of the cooling zone 1202 of the second adsorption runner 120 The cooling gas inlet line 122 is for fresh air or outside air to enter (as shown in FIG. 2 ), and the cooling area 1202 of the second adsorption runner 120 is provided for cooling through the fresh air or outside air. Another second embodiment is the first clean gas discharge line 1 12 is provided with a first clean gas communication line 182, and the other end of the first clean gas communication line 182 is connected to the second cooling gas intake line 122 (as shown in FIG. 3) The gas in the first clean gas discharge line 112 is sent to the cooling area 1202 of the second adsorption runner 120 through the first clean gas communication line 182 for cooling, and the first clean gas communication tube The road 182 is provided with a first clean air communication control valve 1821 (as shown in FIG. 3) to control the air volume of the first clean air communication line 182.

另該一第二脫附濃縮氣體管路125的一端係與該第二吸附轉輸120之脫附區1203的一側A連接，而該第二脫附濃縮氣體管路125的另一端係與一焚燒裝置100連接(如第2圖及第3圖所示)，其中該焚燒裝置100係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第一種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置100乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置100不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置100為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口101及出口102，而該入口101係與該第二脫附濃縮氣體管路125連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第二脫附濃縮氣體管路125來輸送到該蓄熱式焚燒爐(RTO)之入口101，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口102則連接至該煙囪170(如第2圖及第3圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪170來排出，另該第二脫附濃縮氣體管路125係設有一風機1251，以能將脫附濃 縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口101內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the second desorption concentrated gas line 125 is connected to one side A of the desorption zone 1203 of the second adsorption transfer 120, and the other end of the second desorption concentrated gas line 125 is connected to An incineration device 100 is connected (as shown in Figures 2 and 3), wherein the incineration device 100 is a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative type One of the incinerators (RTO), and the illustration of the first implementation structure of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 100 described below is a regenerative incinerator (RTO) However, the incinerator 100 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 100 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 101 and an outlet 102, and the inlet 101 is connected to the second desorption concentrated gas pipeline 125 , So that the desorbed concentrated gas desorbed by high temperature can be transported to the inlet 101 of the regenerative incinerator (RTO) through the second desorbed concentrated gas pipeline 125, so that the desorbed concentrated gas can enter the heat storage High-temperature cracking in the incinerator (RTO) to reduce volatile organic compounds, and the outlet 102 of the regenerative incinerator (RTO) is connected to the chimney 170 (as shown in Figures 2 and 3), In order to discharge the clean gas after high-temperature cracking of organic matter through the chimney 170, and the second desorption concentrated gas pipeline 125 is provided with a fan 1251, so as to be able to concentrate the desorption concentration The compressed gas is pushed and pulled into the inlet 101 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to undergo high-temperature cracking.

而本發明第一種實施架構(如第2圖及第3圖所示)中主要在於該第二吸附轉輪120除了設有吸附區1201、冷卻區1202及脫附區1203外，還設有高溫脫附區1204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪120能恢復其吸附能力，使該第二吸附轉輪120能具有四個區域。而該第二吸附轉輪120之高溫脫附區1204的另一側B係與一第四熱氣輸送管路126的一端連接，且該第四熱氣輸送管路126的另一端係與該第四加熱裝置160連接(如第2圖及第3圖所示)，其中該第四加熱裝置160係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第三熱氣輸送管路124係設有一第三熱氣旁通管路192，該第三熱氣旁通管路192的另一端係與該第四加熱裝置160連接(如第2圖及第3圖所示)，以能將經由該第三加熱裝置150進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路192來輸送到該第四加熱裝置160內，以將進入該第四熱氣輸送管路126內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路126內的高溫熱氣再輸送到該第二吸附轉輪120之高溫脫附區1204，以供進行高溫脫附使用，另該第三熱氣旁通管路192係設有一第三熱氣旁通控制閥門1921(如第3圖所示)，以控制該第三熱氣旁通管路192的風量。 The first implementation structure of the present invention (as shown in FIG. 2 and FIG. 3) mainly lies in that the second adsorption rotor 120 is provided with an adsorption zone 1201, a cooling zone 1202 and a desorption zone 1203, as well as The high-temperature desorption zone 1204 can be used to remove residual high-boiling organic compounds (VOC) during on-line operation (ON LINE), so that the second adsorption rotor 120 can restore its adsorption capacity, so that the second adsorption The runner 120 can have four areas. The other side B of the high temperature desorption zone 1204 of the second adsorption runner 120 is connected to one end of a fourth hot gas delivery line 126, and the other end of the fourth hot gas delivery line 126 is connected to the fourth The heating device 160 is connected (as shown in FIGS. 2 and 3), wherein the fourth heating device 160 is any one of a heater, a pipe heater, or a heat exchanger, and the heater (not shown) is It is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown in the figure) is any one using gas fuel or liquid fuel. The third hot gas delivery pipeline 124 is provided with a third hot gas bypass pipeline 192, and the other end of the third hot gas bypass pipeline 192 is connected to the fourth heating device 160 (as shown in FIGS. 2 and 3) As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the third heating device 150 can be partially diverted and sent to the fourth heating device 160 through the third hot gas bypass line 192 to The high-temperature hot gas entering the fourth hot gas conveying line 126 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the fourth hot gas conveying line 126 is sent to the high temperature of the second adsorption runner 120 The desorption zone 1204 is used for high-temperature desorption, and the third hot gas bypass line 192 is provided with a third hot gas bypass control valve 1921 (as shown in FIG. 3) to control the third hot gas bypass The air volume through the pipeline 192.

再者，該第二吸附轉輪120之高溫脫附區1204的一側A係連接一第二高溫脫附濃縮氣體管路127(如第2圖及第3圖所示)，而該第二高溫脫附濃縮氣體管路127的另一端係與該第二脫附濃縮氣體管路125連接，以將經過該第二吸附轉輪120之高溫脫附區1204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路127來輸送到該第二脫附濃縮氣體管路125內，再透過該第二脫附濃縮氣體管路125輸送到該蓄熱式焚燒爐(RTO)之入口101，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路125內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, a side A of the high temperature desorption zone 1204 of the second adsorption runner 120 is connected to a second high temperature desorption concentrated gas pipeline 127 (as shown in FIGS. 2 and 3), and the second The other end of the high-temperature desorption concentrated gas line 127 is connected to the second desorption concentrated gas line 125 to concentrate the high-temperature desorption concentrated through the high-temperature desorption zone 1204 of the second adsorption runner 120 Gas can be transported into the second desorption concentrated gas line 125 through the second high-temperature desorption concentrated gas line 127, and then transferred to the regenerative incinerator (RTO) through the second desorption concentrated gas line 125 ) Of the inlet 101, allowing the high-temperature desorbed concentrated gas to enter the regenerative incinerator (RTO) together with the desorbed concentrated gas in the second desorbed concentrated gas pipeline 125 for high-temperature cracking.

另本發明第二種實施方式的具高溫脫附之轉輪方法，主要係設有一第一吸附轉輪210、一第二吸附轉輪220、一第一加熱裝置230、一第二加熱裝置240、一第三加熱裝置250及一第四加熱裝置260，而該第一吸附轉輪210係設有吸附區2101、冷卻區2102、脫附區2103及高溫脫附區2104，另該第二吸附轉輪220係設有吸附區2201、冷卻區2202、脫附區2203及高溫脫附區2204，因此，本發明主要在於該第一吸附轉輪210及該第二吸附轉輪220除了設有吸附區2101、2201、冷卻區2102、2202及脫附區2103、2203外，還設有高溫脫附區2104、2204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪210及該第二吸附轉輪220能恢復其吸附能力，使該第一吸附轉輪210及該第二吸附轉輪220能具有四個區域。 In addition, the rotor method with high temperature desorption according to the second embodiment of the present invention is mainly provided with a first adsorption runner 210, a second adsorption runner 220, a first heating device 230, and a second heating device 240 , A third heating device 250 and a fourth heating device 260, and the first adsorption runner 210 is provided with an adsorption zone 2101, a cooling zone 2102, a desorption zone 2103 and a high temperature desorption zone 2104, and the second adsorption The runner 220 is provided with an adsorption zone 2201, a cooling zone 2202, a desorption zone 2203, and a high-temperature desorption zone 2204. Therefore, the present invention mainly lies in that the first adsorption runner 210 and the second adsorption runner 220 are provided with adsorption Zone 2101, 2201, cooling zone 2102, 2202 and desorption zone 2103, 2203, there are also high-temperature desorption zone 2104, 2204, used for online operation (ON LINE), the residual high-boiling organic matter ( VOC) is released, so that the first adsorption runner 210 and the second adsorption runner 220 can restore their adsorption capacity, so that the first adsorption runner 210 and the second adsorption runner 220 can have four regions.

而該第二種實施方式的主要步驟(如第4圖所示)係包括： 步驟S200輸入待吸附之氣體：該第一吸附轉輪210之吸附區2101的一側A係由一廢氣進氣管路211來輸入待吸附之氣體，而該第一吸附轉輪210之吸附區2101的另一側B則透過一第一淨氣排放管路212來輸送經過吸附後之氣體；透過該第一吸附轉輪210之吸附區2101的一側A係連接一廢氣進氣管路211(如第5圖及第6圖所示)，以能由該廢氣進氣管路211來輸入待吸附之氣體，而該待吸附之氣體可以為揮發性有機化合物(VOC)、二氧化碳(CO2)、氮氣(N2)、水氣或氧氣(O2)之其中任一或複數組合之一，也可以是其他上述未表述之氣體，而該第一吸附轉輪210之吸附區2101的另一側B則與該一第一淨氣排放管路212之一端連接(如第5圖及第6圖所示)，讓該待吸附之氣體經該第一吸附轉輪210之吸附區2101進行吸附後再由該第一淨氣排放管路212來輸送經過吸附後之氣體。而完成上述步驟S200後即進行下一步驟S210。 The main steps of this second embodiment (as shown in Figure 4) include: Step S200: Input the gas to be adsorbed: the side A of the adsorption zone 2101 of the first adsorption runner 210 is inputted by a waste gas inlet line 211, and the adsorption zone of the first adsorption runner 210 The other side B of 2101 transports the adsorbed gas through a first clean gas discharge line 212; the side A of the adsorption area 2101 through the first adsorption runner 210 is connected to an exhaust gas inlet line 211 (As shown in Figures 5 and 6), the gas to be adsorbed can be input from the exhaust gas inlet line 211, and the gas to be adsorbed can be volatile organic compounds (VOC), carbon dioxide (CO2) , Nitrogen (N2), water vapor or oxygen (O2) any one or a combination of plural, can also be other gas not mentioned above, and the other side of the adsorption area 2101 of the first adsorption runner 210 B Connected to one end of the first clean gas discharge line 212 (as shown in FIG. 5 and FIG. 6), allowing the gas to be adsorbed to be adsorbed through the adsorption area 2101 of the first adsorption rotor 210 The adsorbed gas is delivered by the first clean gas discharge line 212. After the above step S200 is completed, the next step S210 is performed.

另，下一步進行的步驟S210輸入用來冷卻之氣體：該第一吸附轉輪210之冷卻區2102的另一側B係由一第一冷卻氣進氣管路213來輸入用來冷卻之氣體，而該第一吸附轉輪210之冷卻區2102的一側A則透過一第一冷卻氣輸送管路214來連接至該第一加熱裝置230，以將經過該第一吸附轉輪210之冷卻區2102的氣體輸送到該第一加熱裝置230內；該第一吸附轉輪210之冷卻區2102的另一側B係連接一第一冷卻氣進氣管路213(如第5圖及第6圖所示)，以供用來冷卻之氣體進入該第一吸附轉輪210之冷卻區2102來進行冷卻使用，而該第一吸附轉輪210之冷卻區2102的一側A則連接一 第一冷卻氣輸送管路214(如第5圖及第6圖所示)，該第一冷卻氣輸送管路214的另一端係與該第一加熱裝置230連接，使能將經過該第一吸附轉輪210之冷卻區2102的氣體輸送到該第一加熱裝置230內。 In addition, in the next step S210, the gas used for cooling is input: the other side B of the cooling zone 2102 of the first adsorption runner 210 is inputted by a first cooling gas inlet line 213 for cooling , And the side A of the cooling zone 2102 of the first adsorption runner 210 is connected to the first heating device 230 through a first cooling gas delivery line 214 to cool the first adsorption runner 210 The gas in the zone 2102 is delivered to the first heating device 230; the other side B of the cooling zone 2102 of the first adsorption runner 210 is connected to a first cooling gas inlet line 213 (as shown in FIGS. 5 and 6 As shown in the figure), the gas used for cooling enters the cooling zone 2102 of the first adsorption runner 210 for cooling, and the side A of the cooling zone 2102 of the first adsorption runner 210 is connected to a The first cooling gas delivery line 214 (as shown in Figures 5 and 6), the other end of the first cooling gas delivery line 214 is connected to the first heating device 230, enabling the first The gas in the cooling zone 2102 of the adsorption rotor 210 is delivered into the first heating device 230.

而上述該第一加熱裝置230係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第一吸附轉輪210之冷卻區2102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪210之冷卻區2102的另一側B所連接的第一冷卻氣進氣管路213乃是供新鮮空氣或外氣進入(如第5圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪210之冷卻區2102降溫用。另第二種實施態樣係該第一淨氣排放管路212係設有一第一淨氣連通管路282，而該第一淨氣連通管路282的另一端係與該第一冷卻氣進氣管路213連接(如第6圖所示)，以能透過該第一淨氣連通管路282來將該第一淨氣排放管路212內經過該第一吸附轉輪210之吸附區2101所吸附過後的氣體輸送到該第一吸附轉輪210之冷卻區2102以進行降溫使用，另該第一淨氣連通管路282係設有一第一淨氣連通控制閥門2821(如第6圖所示)，以控制該第一淨氣連通管路282的風量。而完成上述步驟S210後即進行下一步驟S220。 The above-mentioned first heating device 230 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling zone 2102 of the first adsorption runner 210 described above is provided with two implementations, of which the first implementation is the connection of the other side B of the cooling zone 2102 of the first adsorption runner 210 A cooling gas inlet line 213 is for fresh air or outside air to enter (as shown in FIG. 5), and provides cooling temperature of the cooling area 2102 of the first adsorption runner 210 through the fresh air or outside air. In another second embodiment, the first clean gas discharge line 212 is provided with a first clean gas communication line 282, and the other end of the first clean gas communication line 282 is connected to the first cooling gas The gas line 213 is connected (as shown in FIG. 6) so that the first clean gas discharge line 212 can pass through the adsorption area 2101 of the first adsorption runner 210 through the first clean gas communication line 282 The adsorbed gas is sent to the cooling zone 2102 of the first adsorption runner 210 for cooling, and the first clean gas communication line 282 is provided with a first clean gas communication control valve 2821 (as shown in FIG. 6) Shown) to control the air volume of the first clean air communication line 282. After the above step S210 is completed, the next step S220 is performed.

另，下一步進行的步驟S220輸送高溫熱氣進行脫附：該第一吸附轉輪210之脫附區2103的一側A係由一第一熱氣輸送管路 215來輸送該第一加熱裝置230內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路215係設有一第一熱氣旁通管路291，透過該第一熱氣旁通管路291連接至該第二加熱裝置240，而該第一吸附轉輪210之脫附區2103的另一側B則透過一第一脫附濃縮氣體管路216來輸送經過脫附後之脫附濃縮氣體；該第一吸附轉輪210之脫附區2103的一側A係與該一第一熱氣輸送管路215連接，且該第一熱氣輸送管路215的另一端則與該第一加熱裝置230連接(如第5圖及第6圖所示)，以能將經由該第一加熱裝置230進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路215來輸送到該第一吸附轉輪210之脫附區2103來進行脫附使用。另該第一熱氣輸送管路215係設有一第一熱氣旁通管路291，該第一熱氣旁通管路291的另一端係與該第二加熱裝置240連接(如第5圖及第6圖所示)，以能將經由該第一加熱裝置230進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路291來輸送到該第二加熱裝置240內，另該第一吸附轉輪210之脫附區2103的另一側B係連接一第一脫附濃縮氣體管路216的一端(如第5圖及第6圖所示)，以用輸送經過該第一吸附轉輪210之脫附區2103進行脫附後之脫附濃縮氣體。 In addition, in the next step S220, high-temperature hot gas is transported for desorption: the side A of the desorption area 2103 of the first adsorption runner 210 is composed of a first hot gas transport line 215 to transport the high-temperature hot gas generated in the first heating device 230 for desorption, and the first hot gas delivery pipeline 215 is provided with a first hot gas bypass pipeline 291 through which the first hot gas bypass pipeline 291 is connected to the second heating device 240, and the other side B of the desorption zone 2103 of the first adsorption runner 210 is conveyed through a first desorption concentration gas line 216 to the desorption concentration after desorption Gas; one side A of the desorption zone 2103 of the first adsorption runner 210 is connected to the first hot gas delivery pipe 215, and the other end of the first hot gas delivery pipe 215 is connected to the first heating device 230 connection (as shown in FIG. 5 and FIG. 6), so that high-temperature hot gas heated or exchanged by the first heating device 230 can be transported to the first adsorption rotor through the first hot gas transport line 215 The desorption area 2103 of the wheel 210 is used for desorption. In addition, the first hot gas delivery line 215 is provided with a first hot gas bypass line 291, and the other end of the first hot gas bypass line 291 is connected to the second heating device 240 (as shown in FIGS. 5 and 6 As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the first heating device 230 can be partially shunted and sent to the second heating device 240 through the first hot gas bypass line 291, and The other side B of the desorption zone 2103 of the first adsorption runner 210 is connected to one end of a first desorption concentrated gas line 216 (as shown in FIGS. 5 and 6) for transportation through the first The desorption concentrated gas after desorption in the desorption zone 2103 of an adsorption runner 210.

而上述該第二加熱裝置240係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該第一熱氣旁通管路291係設有一第一熱氣旁通控制閥門2911(如第6圖所示)，以控制該第一熱氣旁通管路291的風量， 使能將經由該第一加熱裝置230進行加熱或熱交換的高溫熱氣部分分流到該第二加熱裝置240內。而完成上述步驟S220後即進行下一步驟S230。 The above-mentioned second heating device 240 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. Moreover, the first hot gas bypass line 291 is provided with a first hot gas bypass control valve 2911 (as shown in FIG. 6) to control the air volume of the first hot gas bypass line 291, The high-temperature hot gas heated or exchanged through the first heating device 230 is partially shunted into the second heating device 240. After the above step S220 is completed, the next step S230 is performed.

另，下一步進行的步驟S230再將高沸點有機物脫出：該第一吸附轉輪210之高溫脫附區2104的一側A係由一第二熱氣輸送管路217來輸送由該第二加熱裝置240內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪210之高溫脫附區2104的另一側B則透過一第一高溫脫附濃縮氣體管路218來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路216內；該第一吸附轉輪210之高溫脫附區2104的一側A係與一第二熱氣輸送管路217的一端連接，且該第二熱氣輸送管路217的另一端係與該第二加熱裝置240連接(如第5圖及第6圖所示)，透過該第二加熱裝置240來將進入該第二熱氣輸送管路217內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路217內的高溫熱氣再輸送到該第一吸附轉輪210之高溫脫附區2104，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪210能恢復其吸附能力，另該第一吸附轉輪210之高溫脫附區2104的另一側B係連接一第一高溫脫附濃縮氣體管路218(如第5圖及第6圖所示)，而該第一高溫脫附濃縮氣體管路218的另一端係與該第一脫附濃縮氣體管路216連接，以將經過該第一吸附轉輪210之高溫脫附區2104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路218來輸送到該第一脫附濃縮氣體管路216內。 In addition, the next step S230 is to remove the high-boiling organic matter: the side A of the high-temperature desorption zone 2104 of the first adsorption runner 210 is conveyed by a second hot gas conveying line 217 by the second heating The high temperature hot gas raised to a certain temperature in the device 240 to remove high boiling point organic compounds (VOC), and the other side B of the high temperature desorption zone 2104 of the first adsorption runner 210 is desorbed through a first high temperature The concentrated gas pipeline 218 is used to transport the desorbed concentrated gas after high temperature to the first desorbed concentrated gas pipeline 216; the side A of the high temperature desorption zone 2104 of the first adsorption runner 210 is connected to a One end of the second hot gas delivery line 217 is connected, and the other end of the second hot gas delivery line 217 is connected to the second heating device 240 (as shown in FIGS. 5 and 6), through which the second heating Device 240 is used to raise the high-temperature hot gas entering the second hot gas delivery pipeline 217 to a certain temperature (for example, 300°C), and then deliver the high-temperature hot gas in the second hot gas delivery pipeline 217 to the first adsorption runner The high-temperature desorption zone 2104 of 210 is used for high-temperature desorption. When online operation (ON LINE), the remaining high-boiling organic matter (VOC) can be removed, so that the first adsorption runner 210 can restore it Adsorption capacity, and the other side B of the high temperature desorption zone 2104 of the first adsorption runner 210 is connected to a first high temperature desorption concentrated gas pipeline 218 (as shown in FIGS. 5 and 6), and the The other end of the first high temperature desorption concentrated gas line 218 is connected to the first desorption concentrated gas line 216 to desorb the high temperature desorbed by the high temperature desorption zone 2104 of the first adsorption runner 210 The attached concentrated gas can be transported into the first desorbed concentrated gas line 216 through the first high-temperature desorbed concentrated gas line 218.

而上述該第一脫附濃縮氣體管路216的另一端係與一焚燒裝置200連接(如第5圖及第6圖所示)，其中該焚燒裝置200係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第二種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置200乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置200不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置200為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口201及出口202，而該入口201係與該第一脫附濃縮氣體管路216連接，其中該第一脫附濃縮氣體管路216另有與該第一高溫脫附濃縮氣體管路218的另一端連接，以將經過該第一吸附轉輪210之高溫脫附區2104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路218來輸送到該第一脫附濃縮氣體管路216內，使該第一脫附濃縮氣體管路216內除了經過該第一吸附轉輪210之脫附區2103所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路216內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口202則連接至一煙囪270(如第5圖及第6圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪270來排出，另該第一脫附濃縮氣體管路216係設有一風機2161(如第6圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口201內，讓脫附濃縮氣體能進行高溫裂解。而完成上述步驟S230後即進行下一步驟S240。 The other end of the first desorption concentrated gas pipeline 216 is connected to an incinerator 200 (as shown in FIGS. 5 and 6), wherein the incinerator 200 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown), or regenerative incinerator (RTO), and the illustration of the second embodiment of the present invention takes the regenerative incinerator (RTO) as an example, Moreover, the incinerator 200 described below is a regenerative incinerator (RTO), but the incinerator 200 of the present invention is not limited to a regenerative incinerator (RTO), but may also be a direct combustion incinerator (TO) (Figure Not shown) or catalyst furnace (not shown). When the incinerator 200 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 201 and an outlet 202, and the inlet 201 is connected to the first desorption concentrated gas pipeline 216 , Wherein the first desorption concentrated gas pipeline 216 is additionally connected to the other end of the first high-temperature desorption concentrated gas pipeline 218 to desorb the high-temperature desorption zone 2104 passing through the first adsorption runner 210 The lower high-temperature desorption concentrated gas can be transported into the first desorption concentrated gas line 216 through the first high-temperature desorption concentrated gas line 218, so that the first desorption concentrated gas line 216 passes through the The desorption concentrated gas desorbed by the desorption zone 2103 of the first adsorption runner 210 also contains high-temperature desorption concentrated gas, so that the high-temperature desorption concentrated gas can be desorbed from the first desorption concentrated gas pipeline 216 The concentrated gas enters the regenerative incinerator (RTO) for high temperature cracking to reduce volatile organic compounds, and the outlet 202 of the regenerative incinerator (RTO) is connected to a chimney 270 (as shown in Figure 5 and (Figure 6), so that the clean gas after pyrolysis of organic compounds can be discharged through the chimney 270, and the first desorption concentrated gas pipeline 216 is provided with a fan 2161 (as shown in Figure 6) In order to push and pull the desorbed concentrated gas into the inlet 201 of the regenerative incinerator (RTO), the desorbed concentrated gas can be pyrolyzed at high temperature. After the above step S230 is completed, the next step S240 is performed.

另，下一步進行的步驟S240輸送欲再吸附之氣體：該第二吸附轉輪220之吸附區2201的一側A係由該第一淨氣排放管路212來輸送欲進行再吸附之氣體，而該第二吸附轉輪220之吸附區2201的另一側B則透過一第二淨氣排放管路221來輸送經過再吸附後之氣體；該第二吸附轉輪220之吸附區2201的一側A係與該第一淨氣排放管路212的另一端相連接(如第5圖及第6圖所示)，使該第一淨氣排放管路212內經過吸附後之氣體能直接再輸送到該第二吸附轉輪220之吸附區2201內進行再吸附，另該第二吸附轉輪220之吸附區2201的另一側B係連接一第二淨氣排放管路221，並透過該第二淨氣排放管路221來輸送經過再吸附後之氣體。 In addition, the next step S240 conveys the gas to be re-adsorbed: the side A of the adsorption area 2201 of the second adsorption rotor 220 is conveyed by the first clean gas discharge line 212 to the gas to be re-adsorbed, The other side B of the adsorption zone 2201 of the second adsorption runner 220 conveys the re-adsorbed gas through a second clean gas discharge line 221; one of the adsorption zones 2201 of the second adsorption runner 220 Side A is connected to the other end of the first clean gas discharge line 212 (as shown in FIGS. 5 and 6), so that the adsorbed gas in the first clean gas discharge line 212 can be directly recycled It is sent to the adsorption zone 2201 of the second adsorption runner 220 for re-adsorption, and the other side B of the adsorption zone 2201 of the second adsorption runner 220 is connected to a second clean gas discharge line 221 and passes through the The second clean gas discharge line 221 conveys the gas after re-adsorption.

而上述該第二淨氣排放管路221之另一端則與一煙囪270連接(如第5圖及第6圖所示)，以方便將經由該第一吸附轉輪210之吸附區2101及該第二吸附轉輪220之吸附區2201所吸附過後之氣體透過該煙囪270來進行排放，其中該第二淨氣排放管路221係設有一風機2211(如第6圖所示)，以增加氣體之流速來流向該煙囪270。而完成上述步驟S240後即進行下一步驟S250。 The other end of the second clean gas discharge line 221 is connected to a chimney 270 (as shown in FIG. 5 and FIG. 6 ), so as to facilitate the passage of the adsorption zone 2101 through the first adsorption runner 210 and the The gas adsorbed by the adsorption area 2201 of the second adsorption runner 220 is discharged through the chimney 270, wherein the second clean gas discharge line 221 is provided with a fan 2211 (as shown in FIG. 6) to increase the gas The flow velocity comes to the chimney 270. After the above step S240 is completed, the next step S250 is performed.

另，下一步進行的步驟S250輸入用來冷卻之氣體：該第二吸附轉輪220之冷卻區2202的另一側B係由一第二冷卻氣進氣管路222來輸入用來冷卻之氣體，而該第二吸附轉輪220之冷卻區2202的一側A則透過一第二冷卻氣輸送管路223來連接至該第三加熱裝置250，以將經過該第二吸附轉輪220之冷卻區2202的氣體輸送到該第三加熱裝置250內；該第二吸附轉輪220之冷卻區2202的 另一側B係連接一第二冷卻氣進氣管路222(如第5圖及第6圖所示)，以供用來冷卻之氣體進入該第二吸附轉輪220之冷卻區2202來進行冷卻使用，而該第二吸附轉輪220之冷卻區2202的一側A則連接一第二冷卻氣輸送管路223(如第5圖及第6圖所示)，該第二冷卻氣輸送管路223的另一端係與該第三加熱裝置250連接，使能將經過該第二吸附轉輪220之冷卻區2202的氣體輸送到該第三加熱裝置250內。 In addition, in the next step S250, the gas used for cooling is input: the other side B of the cooling zone 2202 of the second adsorption runner 220 is supplied with a gas for cooling by a second cooling gas inlet line 222 , And the side A of the cooling zone 2202 of the second adsorption runner 220 is connected to the third heating device 250 through a second cooling gas delivery pipe 223 to cool the passing of the second adsorption runner 220 The gas in zone 2202 is delivered to the third heating device 250; the cooling zone 2202 of the second adsorption runner 220 The other side B is connected to a second cooling gas inlet line 222 (as shown in Figures 5 and 6) for the gas used for cooling to enter the cooling zone 2202 of the second adsorption runner 220 for cooling Used, and the side A of the cooling zone 2202 of the second adsorption runner 220 is connected to a second cooling gas delivery line 223 (as shown in FIGS. 5 and 6), the second cooling gas delivery line The other end of 223 is connected to the third heating device 250 to enable the gas passing through the cooling zone 2202 of the second adsorption runner 220 to be transferred into the third heating device 250.

而上述該第三加熱裝置250係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第二吸附轉輪220之冷卻區2202係設有兩種實施態樣，其中第一種實施態樣為該第二吸附轉輪之220冷卻區2202的另一側B所連接的第二冷卻氣進氣管路222乃是供新鮮空氣或外氣進入(如第5圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪220之冷卻區2202降溫用。另第二種實施態樣係該第二淨氣排放管路221係設有一第二淨氣連通管路283，而該第二淨氣連通管路283的另一端係與該第二冷卻氣進氣管路222連接(如第6圖所示)，以能透過該第二淨氣連通管路283來將該第二淨氣排放管路221內的氣體輸送到該第二吸附轉輪220之冷卻區2202以進行降溫使用，另該第二淨氣連通管路283係設有一第二淨氣連通控制閥門2831(如第6圖所示)，以控制該第二淨氣連通管路283的風量。而完成上述步驟S250後即進行下一步驟S260。 The above-mentioned third heating device 250 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling zone 2202 of the second adsorption runner 220 described above is provided with two implementation forms, of which the first implementation form is a third section connected to the other side B of the cooling zone 2202 of the second adsorption runner 220 The second cooling gas inlet line 222 is for fresh air or outside air to enter (as shown in FIG. 5), and provides cooling temperature 2202 of the second adsorption runner 220 through the fresh air or outside air for cooling. In another second embodiment, the second clean gas discharge line 221 is provided with a second clean gas communication line 283, and the other end of the second clean gas communication line 283 is connected to the second cooling gas The gas line 222 is connected (as shown in FIG. 6) so that the gas in the second clean gas discharge line 221 can be sent to the second adsorption runner 220 through the second clean gas communication line 283 The cooling zone 2202 is used for cooling. In addition, the second clean air communication line 283 is provided with a second clean air communication control valve 2831 (as shown in FIG. 6) to control the second clean air communication line 283. Air volume. After the above step S250 is completed, the next step S260 is performed.

另，下一步進行的步驟S260輸送高溫熱氣進行脫附：該第二吸附轉輪220之脫附區2203的一側A係由一第三熱氣輸送管路224來輸送該第三加熱裝置250內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路224係設有一第三熱氣旁通管路292，透過該第三熱氣旁通管路292連接至該第四加熱裝置260，而該第二吸附轉輪220之脫附區2203的另一側B則透過一第二脫附濃縮氣體管路225來輸送經過脫附後之脫附濃縮氣體；該第二吸附轉輪220之脫附區2203的一側A係與該一第三熱氣輸送管路224連接，且該第三熱氣輸送管路224的另一端則與該第三加熱裝置250連接(如第5圖及第6圖所示)，以能將經由該第三加熱裝置250進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路224來輸送到該第二吸附轉輪220之脫附區2203來進行脫附使用。另該第三熱氣輸送管路224係設有一第三熱氣旁通管路292(如第5圖及第6圖所示)，該第三熱氣旁通管路292的另一端係與該第四加熱裝置260連接，以能將經由該第三加熱裝置250進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路292來輸送到該第四加熱裝置260內，另該第二吸附轉輪220之脫附區2203的另一側B係連接一第二脫附濃縮氣體管路225的一端(如第5圖及第6圖所示)，以用輸送經過該第二吸附轉輪220之脫附區2203進行脫附後之脫附濃縮氣體。 In addition, the next step S260 is to transport high-temperature hot gas for desorption: the side A of the desorption zone 2203 of the second adsorption runner 220 is transported into the third heating device 250 by a third hot gas delivery pipeline 224 The generated high-temperature hot gas is used for desorption, and the third hot gas delivery pipeline 224 is provided with a third hot gas bypass pipeline 292, which is connected to the fourth heating device 260 through the third hot gas bypass pipeline 292, The other side B of the desorption zone 2203 of the second adsorption runner 220 conveys the desorbed concentrated gas after desorption through a second desorption concentrated gas line 225; One side A of the desorption zone 2203 is connected to the third hot gas delivery pipe 224, and the other end of the third hot gas delivery pipe 224 is connected to the third heating device 250 (as shown in FIGS. 5 and 6 (Shown in the figure), the high-temperature hot gas heated or exchanged by the third heating device 250 can be transported to the desorption area 2203 of the second adsorption runner 220 through the third hot gas delivery pipe 224 for desorption Attached to use. In addition, the third hot gas delivery line 224 is provided with a third hot gas bypass line 292 (as shown in FIGS. 5 and 6), and the other end of the third hot gas bypass line 292 is connected to the fourth The heating device 260 is connected so that the high-temperature hot gas that is heated or exchanged through the third heating device 250 can be partially shunted, and is transferred into the fourth heating device 260 through the third hot gas bypass line 292, and The other side B of the desorption zone 2203 of the second adsorption runner 220 is connected to one end of a second desorption concentrated gas pipeline 225 (as shown in FIG. 5 and FIG. 6) for transportation through the first The desorption concentrated gas after the desorption zone 2203 of the second adsorption runner 220 performs desorption.

而上述該第四加熱裝置260係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中 任一。且上述該第三熱氣旁通管路292係設有一第三熱氣旁通控制閥門2921(如第6圖所示)，以控制該第三熱氣旁通管路292的風量，使能將經由該第三加熱裝置250進行加熱或熱交換的高溫熱氣部分分流到該第四加熱裝置260內。而完成上述步驟S260後即進行下一步驟S270。 The above-mentioned fourth heating device 260 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is one of gas fuel or liquid fuel Either. And the third hot gas bypass line 292 is provided with a third hot gas bypass control valve 2921 (as shown in FIG. 6) to control the air volume of the third hot gas bypass line 292, enabling The high-temperature hot gas that is heated or exchanged by the third heating device 250 is partially shunted into the fourth heating device 260. After the above step S260 is completed, the next step S270 is performed.

另，下一步進行的步驟S270再將高沸點有機物脫出：該第二吸附轉輪220之高溫脫附區2204的一側A係由一第四熱氣輸送管路226來輸送由該第四加熱裝置260內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪220之高溫脫附區2204的另一側B則透過一第二高溫脫附濃縮氣體管路227來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路225內；該第二吸附轉輪220之高溫脫附區2204的一側A係與一第四熱氣輸送管路226的一端連接，且該第四熱氣輸送管路226的另一端係與該第四加熱裝置260連接(如第5圖及第6圖所示)，透過該第四加熱裝置260來將進入該第四熱氣輸送管路226內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路226內的高溫熱氣再輸送到該第二吸附轉輪220之高溫脫附區2204，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪220能恢復其吸附能力，另該第二吸附轉輪220之高溫脫附區2204的另一側B係連接一第二高溫脫附濃縮氣體管路227(如第5圖及第6圖所示)，而該第二高溫脫附濃縮氣體管路227的另一端係與該第二脫附濃縮氣體管路225連接，以將經過該第二吸附轉輪220 之高溫脫附區2204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路227來輸送到該第二脫附濃縮氣體管路225內。 In addition, in the next step S270, high-boiling organics are removed again: the side A of the high-temperature desorption zone 2204 of the second adsorption runner 220 is conveyed by a fourth hot gas conveying line 226 The high temperature hot gas raised to a certain temperature in the device 260 to remove high boiling point organic compounds (VOC), and the other side B of the high temperature desorption zone 2204 of the second adsorption runner 220 is desorbed through a second high temperature The concentrated gas pipeline 227 is used to transport the desorbed concentrated gas after high temperature to the second desorbed concentrated gas pipeline 225; the side A of the high temperature desorption zone 2204 of the second adsorption runner 220 is connected to a One end of the fourth hot gas delivery line 226 is connected, and the other end of the fourth hot gas delivery line 226 is connected to the fourth heating device 260 (as shown in FIGS. 5 and 6), through which the fourth heating The device 260 raises the high-temperature hot gas entering the fourth hot gas delivery pipeline 226 to a certain temperature (for example, 300°C), and then delivers the high-temperature hot gas in the fourth hot gas delivery pipeline 226 to the second adsorption runner The high-temperature desorption zone 2204 of 220 is used for high-temperature desorption. When online operation (ON LINE), the remaining high-boiling organic matter (VOC) can be removed, so that the second adsorption runner 220 can restore it Adsorption capacity, and the other side B of the high temperature desorption zone 2204 of the second adsorption runner 220 is connected to a second high temperature desorption concentrated gas pipeline 227 (as shown in FIGS. 5 and 6), and the The other end of the second high-temperature desorption concentrated gas line 227 is connected to the second desorption concentrated gas line 225 to pass the second adsorption runner 220 The high-temperature desorption concentrated gas desorbed by the high-temperature desorption zone 2204 can be transported into the second desorption concentrated gas line 225 through the second high-temperature desorption concentrated gas line 227.

而上述該第二脫附濃縮氣體管路225的另一端係與一焚燒裝置200連接(如第5圖及第6圖所示)，其中該焚燒裝置200係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第二種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置200乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置200不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置200為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口201及出口202，而該入口201係與該第二脫附濃縮氣體管路225連接，其中該第二脫附濃縮氣體管路225另有與該第二高溫脫附濃縮氣體管路227的另一端連接，以將經過該第二吸附轉輪220之高溫脫附區2204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路227來輸送到該第二脫附濃縮氣體管路225內，使該第二脫附濃縮氣體管路225內除了經過該第二吸附轉輪220之脫附區2203所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路225內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口202則連接至一煙囪270(如第5圖及第6圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪270來排出，另該第二脫附濃縮氣體管路225係設有一風機2251(如第6圖所示)，以能將脫附濃縮 氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口201內，讓脫附濃縮氣體能進行高溫裂解。 The other end of the second desorbed concentrated gas pipeline 225 is connected to an incinerator 200 (as shown in FIGS. 5 and 6), wherein the incinerator 200 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown), or regenerative incinerator (RTO), and the illustration of the second embodiment of the present invention takes the regenerative incinerator (RTO) as an example, Moreover, the incinerator 200 described below is a regenerative incinerator (RTO), but the incinerator 200 of the present invention is not limited to a regenerative incinerator (RTO), but may also be a direct combustion incinerator (TO) (Figure Not shown) or catalyst furnace (not shown). When the incinerator 200 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 201 and an outlet 202, and the inlet 201 is connected to the second desorption concentrated gas pipeline 225 , Wherein the second desorption concentrated gas pipeline 225 is additionally connected to the other end of the second high-temperature desorption concentrated gas pipeline 227 to desorb the high-temperature desorption zone 2204 passing through the second adsorption runner 220 The lower high-temperature desorption concentrated gas can be transported into the second desorption concentrated gas line 225 through the second high-temperature desorption concentrated gas line 227, so that the second desorption concentrated gas line 225 passes through the The desorption concentrated gas desorbed by the desorption zone 2203 of the second adsorption runner 220 also contains high-temperature desorption concentrated gas, so that the high-temperature desorption concentrated gas can be desorbed from the second desorption concentrated gas pipeline 225 The concentrated gas enters the regenerative incinerator (RTO) for high temperature cracking to reduce volatile organic compounds, and the outlet 202 of the regenerative incinerator (RTO) is connected to a chimney 270 (as shown in Figure 5 and (Figure 6), so that the clean gas after pyrolysis of organic compounds can be discharged through the chimney 270, and the second desorption concentrated gas pipeline 225 is provided with a fan 2251 (as shown in Figure 6) So that desorption can be concentrated The gas is pushed and pulled into the inlet 201 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to undergo high-temperature cracking.

另本發明第二種實施架構的具高溫脫附之轉輪系統(如第5圖及第6圖所示)，主要係透過一第一吸附轉輪210、一第二吸附轉輪220、一第一加熱裝置230、一第二加熱裝置240、一第三加熱裝置250及一第四加熱裝置260之組合設計，而本發明第二種實施架構的第一吸附轉輪210係設有吸附區2101、冷卻區2102、脫附區2103及高溫脫附區2104，該第一吸附轉輪210係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且一廢氣進氣管路211係連接至該第一吸附轉輪210之吸附區2101的一側A(如第5圖及第6圖所示)，以使該第一吸附轉輪210之吸附區2101能吸附該廢氣進氣管路211內的有機物，而該第一吸附轉輪210之吸附區2101的另一側B係與該一第一淨氣排放管路212之一端連接，讓該廢氣經該第一吸附轉輪210之吸附區2101進行吸附有機物後再由該第一淨氣排放管路212來輸送。 In addition, the second embodiment of the present invention of the high-temperature desorption rotor system (as shown in Figures 5 and 6), mainly through a first adsorption runner 210, a second adsorption runner 220, a The combined design of the first heating device 230, a second heating device 240, a third heating device 250 and a fourth heating device 260, and the first adsorption runner 210 of the second embodiment of the present invention is provided with an adsorption area 2101, cooling zone 2102, desorption zone 2103, and high temperature desorption zone 2104, the first adsorption runner 210 is a zeolite concentration runner or a concentration runner of other materials, and an exhaust gas intake line 211 is connected to One side A (as shown in FIGS. 5 and 6) of the adsorption zone 2101 of the first adsorption runner 210, so that the adsorption zone 2101 of the first adsorption runner 210 can adsorb the exhaust gas intake line 211 Organic matter inside, and the other side B of the adsorption zone 2101 of the first adsorption runner 210 is connected to one end of the first clean gas discharge line 212 to allow the exhaust gas to be adsorbed by the first adsorption runner 210 The area 2101 is transported by the first clean gas discharge line 212 after adsorbing organic matter.

另該第一吸附轉輪210之冷卻區2102的另一側B係連接一第一冷卻氣進氣管路213(如第5圖及第6圖所示)，以供氣體進入該第一吸附轉輪210之冷卻區2102來進行冷卻使用，而該第一吸附轉輪210之冷卻區2102的一側A係連接一第一冷卻氣輸送管路214(如第5圖及第6圖所示)，該第一冷卻氣輸送管路214的另一端係與該第一加熱裝置230連接，其中該第一加熱裝置230係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電 熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第一熱氣輸送管路215的一端係與該第一吸附轉輪210之脫附區2103的一側A連接(如第5圖及第6圖所示)，且該第一熱氣輸送管路215的另一端則與該第一加熱裝置230連接，以能將經由該第一加熱裝置230進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路215來輸送到該第一吸附轉輪210之脫附區2103來進行脫附使用。 In addition, the other side B of the cooling zone 2102 of the first adsorption runner 210 is connected to a first cooling gas inlet line 213 (as shown in FIGS. 5 and 6) for the gas to enter the first adsorption The cooling zone 2102 of the runner 210 is used for cooling, and one side A of the cooling zone 2102 of the first adsorption runner 210 is connected to a first cooling gas delivery line 214 (as shown in FIGS. 5 and 6) ), the other end of the first cooling gas delivery line 214 is connected to the first heating device 230, wherein the first heating device 230 is any one of a heater, a pipe heater or a heat exchanger, the heating The device (not shown) is a heating wire, electric Either a heat pipe or an electric heating plate, the pipe heater (not shown) is either gas fuel or liquid fuel. One end of the first hot gas delivery pipe 215 is connected to the side A of the desorption area 2103 of the first adsorption runner 210 (as shown in FIGS. 5 and 6), and the first hot gas delivery The other end of the pipeline 215 is connected to the first heating device 230, so that the high-temperature hot gas heated or exchanged by the first heating device 230 can be transported to the first adsorption through the first hot gas delivery pipeline 215 The desorption area 2103 of the runner 210 is used for desorption.

而上述該第一吸附轉輪210之冷卻區2102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪210之冷卻區2102的另一側B所連接的第一冷卻氣進氣管路213乃是供新鮮空氣或外氣進入(如第5圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪210之冷卻區2102降溫用。另第二種實施態樣係該第一淨氣排放管路212係設有一第一淨氣連通管路282，而該第一淨氣連通管路282的另一端係與該第一冷卻氣進氣管路213連接(如第6圖所示)，以能透過該第一淨氣連通管路282來將該第一淨氣排放管路212內經過該第一吸附轉輪210之吸附區2101所吸附過後的氣體輸送到該第一吸附轉輪210之冷卻區2102以進行降溫使用，另該第一淨氣連通管路282係設有一第一淨氣連通控制閥門2821(如第6圖所示)，以控制該第一淨氣連通管路282的風量。 The cooling zone 2102 of the first adsorption runner 210 described above is provided with two implementation forms, of which the first implementation form is the third side connected to the other side B of the cooling zone 2102 of the first adsorption runner 210 A cooling gas inlet line 213 is for fresh air or outside air to enter (as shown in FIG. 5), and provides cooling temperature of the cooling area 2102 of the first adsorption runner 210 through the fresh air or outside air. In another second embodiment, the first clean gas discharge line 212 is provided with a first clean gas communication line 282, and the other end of the first clean gas communication line 282 is connected to the first cooling gas The gas line 213 is connected (as shown in FIG. 6) so that the first clean gas discharge line 212 can pass through the adsorption area 2101 of the first adsorption runner 210 through the first clean gas communication line 282 The adsorbed gas is sent to the cooling zone 2102 of the first adsorption runner 210 for cooling, and the first clean gas communication line 282 is provided with a first clean gas communication control valve 2821 (as shown in FIG. 6) Shown) to control the air volume of the first clean air communication line 282.

另該一第一脫附濃縮氣體管路216的一端係與該第一吸附轉輪210之脫附區2103的另一側B連接，而該第一脫附濃縮氣體管路216的另一端係與一焚燒裝置200連接(如第5圖及第6圖所 示)，其中該焚燒裝置200係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第二種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置200乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置200不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置200為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口201及出口202，而該入口201係與該第一脫附濃縮氣體管路216連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第一脫附濃縮氣體管路216來輸送到該蓄熱式焚燒爐(RTO)之入口201，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口202則連接至一煙囪270(如第5圖及第6圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪270來排出，另該第一脫附濃縮氣體管路216係設有一風機2161，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口201內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the first desorption concentrated gas line 216 is connected to the other side B of the desorption zone 2103 of the first adsorption runner 210, and the other end of the first desorption concentrated gas line 216 is Connected to an incinerator 200 (as shown in Figures 5 and 6) Shown), wherein the incineration device 200 is any one of a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative incinerator (RTO), and the second invention The illustration of this kind of implementation architecture takes the regenerative incinerator (RTO) as an example, and the incinerator 200 described below is a regenerative incinerator (RTO), but the incinerator 200 of the present invention does not use a regenerative incinerator ( RTO) is limited, it can also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 200 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 201 and an outlet 202, and the inlet 201 is connected to the first desorption concentrated gas pipeline 216 , So that the desorbed concentrated gas desorbed through high temperature can be transported to the inlet 201 of the regenerative incinerator (RTO) through the first desorbed concentrated gas pipeline 216, so that the desorbed concentrated gas can enter the heat storage Pyrolysis in the incinerator (RTO) to reduce volatile organic compounds, and the outlet 202 of the regenerative incinerator (RTO) is connected to a chimney 270 (as shown in Figures 5 and 6), In order to discharge the clean gas after high-temperature pyrolysis of organic matter through the chimney 270, the first desorption concentrated gas pipeline 216 is provided with a fan 2161 to push and pull the desorbed concentrated gas into the regenerative incinerator In the inlet 201 of (RTO), the desorbed concentrated gas can be cracked at high temperature.

而本發明第二種實施架構(如第5圖及第6圖所示)中主要在於該第一吸附轉輪210除了設有吸附區2101、冷卻區2102及脫附區2103外，還設有高溫脫附區2104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪210能恢復其吸附能力，使該第一吸附轉輪210能具有四個區域。而該第一吸附轉輪210之高溫脫附區2104的一側A係與一第二熱氣輸送管路217的一端連接，且該第二熱氣輸送管路217的另一端係與該 第二加熱裝置240連接(如第5圖及第6圖所示)，其中該第二加熱裝置240係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第一熱氣輸送管路215係設有一第一熱氣旁通管路291，該第一熱氣旁通管路291的另一端係與該第二加熱裝置240連接(如第5圖及第6圖所示)，以能將經由該第一加熱裝置230進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路291來輸送到該第二加熱裝置240內，以將進入該第二熱氣輸送管路217內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路217內的高溫熱氣再輸送到該第一吸附轉輪210之高溫脫附區2104，以供進行高溫脫附使用，另該第一熱氣旁通管路291係設有一第一熱氣旁通控制閥門2911(如第6圖所示)，以控制該第一熱氣旁通管路291的風量。 The second implementation structure of the present invention (as shown in FIG. 5 and FIG. 6) is mainly that the first adsorption rotor 210 is provided with an adsorption zone 2101, a cooling zone 2102 and a desorption zone 2103, and The high-temperature desorption zone 2104 can be used to remove residual high-boiling organic compounds (VOC) during on-line operation (ON LINE), so that the first adsorption runner 210 can restore its adsorption capacity, so that the first adsorption The runner 210 can have four areas. One side A of the high-temperature desorption zone 2104 of the first adsorption runner 210 is connected to one end of a second hot gas delivery pipe 217, and the other end of the second hot gas delivery pipe 217 is connected to the The second heating device 240 is connected (as shown in FIGS. 5 and 6), wherein the second heating device 240 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown in the figure) ) Is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown) is any of gas fuel or liquid fuel. The first hot gas delivery line 215 is provided with a first hot gas bypass line 291, and the other end of the first hot gas bypass line 291 is connected to the second heating device 240 (as shown in FIGS. 5 and 6 As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the first heating device 230 can be partially diverted and sent to the second heating device 240 through the first hot gas bypass line 291 to The high-temperature hot gas entering the second hot gas conveying line 217 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the second hot gas conveying line 217 is then sent to the high temperature of the first adsorption runner 210 The desorption zone 2104 is used for high temperature desorption. In addition, the first hot gas bypass line 291 is provided with a first hot gas bypass control valve 2911 (as shown in FIG. 6) to control the first hot gas bypass The air volume through the pipeline 291.

再者，該第一吸附轉輪210之高溫脫附區2104的另一側B係連接一第一高溫脫附濃縮氣體管路218(如第5圖及第6圖所示)，而該第一高溫脫附濃縮氣體管路218的另一端係與該第一脫附濃縮氣體管路216連接，以將經過該第一吸附轉輪210之高溫脫附區2104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路218來輸送到該第一脫附濃縮氣體管路216內，再透過該第一脫附濃縮氣體管路216輸送到該蓄熱式焚燒爐(RTO)之入口201，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路216內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, the other side B of the high temperature desorption zone 2104 of the first adsorption runner 210 is connected to a first high temperature desorption concentrated gas pipeline 218 (as shown in FIGS. 5 and 6), and the first The other end of a high-temperature desorption concentrated gas line 218 is connected to the first desorption concentrated gas line 216 to desorb the high-temperature desorbed through the high-temperature desorption area 2104 of the first adsorption runner 210 The concentrated gas can be transported into the first desorption concentrated gas line 216 through the first high-temperature desorption concentrated gas line 218, and then transferred to the regenerative incinerator through the first desorption concentrated gas line 216 ( The inlet 201 of the RTO) allows the high-temperature desorbed concentrated gas to enter the regenerative incinerator (RTO) together with the desorbed concentrated gas in the first desorbed concentrated gas line 216 for high-temperature cracking.

另該第二吸附轉輪220係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且該第二吸附轉輪220內係設有吸附區2201、冷卻區2202、脫附區2203及高溫脫附區2204，而該第二吸附轉輪220之吸附區2201的一側A係與該第一淨氣排放管路212的另一端相連接(如第5圖及第6圖所示)，使該第一淨氣排放管路212內的氣體能直接再輸送到該第二吸附轉輪220之吸附區2201內進行吸附，另該第二吸附轉輪220之吸附區2201的另一側B係連接一第二淨氣排放管路221，而該第二淨氣排放管路221之另一端則與一煙囪270連接(如第5圖及第6圖所示)，以方便將經由該第一吸附轉輪210之吸附區2101及該第二吸附轉輪220之吸附區2201所吸附過的氣體透過該煙囪270來進行排放，其中該第二淨氣排放管路221係設有一風機2211(如第6圖所示)，以增加氣體之流速來流向該煙囪270。 In addition, the second adsorption runner 220 is a zeolite concentration runner or a concentration runner of other materials, and the second adsorption runner 220 is provided with an adsorption zone 2201, a cooling zone 2202, a desorption zone 2203 and a high temperature desorption Attached area 2204, and one side A of the adsorption area 2201 of the second adsorption runner 220 is connected to the other end of the first clean gas discharge line 212 (as shown in FIGS. 5 and 6), so that The gas in the first clean gas discharge line 212 can be directly sent to the adsorption zone 2201 of the second adsorption runner 220 for adsorption, and the other side of the adsorption zone 2201 of the second adsorption runner 220 is B A second clean gas discharge line 221 is connected, and the other end of the second clean gas discharge line 221 is connected to a chimney 270 (as shown in FIG. 5 and FIG. 6) to facilitate the passage of the first The gas adsorbed by the adsorption area 2101 of the adsorption rotor 210 and the adsorption area 2201 of the second adsorption rotor 220 is discharged through the chimney 270, wherein the second clean gas discharge line 221 is provided with a fan 2211 (such as (Shown in Figure 6), the gas flow rate is increased to the chimney 270.

另該第二吸附轉輪220之冷卻區2202的另一側B係連接一第二冷卻氣進氣管路222，以供氣體進入該第二吸附轉輪220之冷卻區2202來進行冷卻使用，而該第二吸附轉輪220之冷卻區2202的一側A係連接一第二冷卻氣輸送管路223(如第5圖及第6圖所示)，該第二冷卻氣輸送管路223的另一端係與該第三加熱裝置250連接，其中該第三加熱裝置250係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第三熱氣輸送管路224的一端係與該第二吸附轉輪220之脫附區2203的一側A連接，且該第三熱氣輸送管路224的另一端係與該第三 加熱裝置250連接(如第5圖及第6圖所示)，以能將經由該第三加熱裝置250進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路224來輸送到該第二吸附轉輪220之脫附區2203來進行脫附使用。 In addition, the other side B of the cooling zone 2202 of the second adsorption runner 220 is connected to a second cooling gas inlet line 222 for the gas to enter the cooling zone 2202 of the second adsorption runner 220 for cooling. A side A of the cooling zone 2202 of the second adsorption runner 220 is connected to a second cooling gas delivery line 223 (as shown in FIGS. 5 and 6). The other end is connected to the third heating device 250, wherein the third heating device 250 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is an electric heating wire or an electric heater Either a tube or an electric heating plate, the pipe heater (not shown) is either gas fuel or liquid fuel. One end of the third hot gas delivery pipe 224 is connected to one side A of the desorption zone 2203 of the second adsorption runner 220, and the other end of the third hot gas delivery pipe 224 is connected to the third The heating device 250 is connected (as shown in FIG. 5 and FIG. 6 ), so that the high-temperature hot gas heated or exchanged through the third heating device 250 can be transported to the second through the third hot gas delivery line 224 The desorption area 2203 of the adsorption rotor 220 is used for desorption.

而上述該第二吸附轉輪220之冷卻區2202係設有兩種實施態樣，其中第一種實施態樣為該第二吸附轉輪220之冷卻區2202的另一側B所連接的第二冷卻氣進氣管路222乃是供新鮮空氣或外氣進入(如第5圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪220之冷卻區2202降溫用。另第二種實施方式係該第二淨氣排放管路221係設有一第二淨氣連通管路283，而該第二淨氣連通管路283的另一端係與該第二冷卻氣進氣管路222連接(如第6圖所示)，以能透過該第二淨氣連通管路283來將該第二淨氣排放管路221內的氣體輸送到該第二吸附轉輪220之冷卻區2202以進行降溫使用，另該第二淨氣連通管路283係設有一第二淨氣連通控制閥門2831(如第6圖所示)，以控制該第二淨氣連通管路283的風量。 The cooling zone 2202 of the second adsorption runner 220 is provided with two implementations, of which the first implementation is the connection of the second side B of the cooling zone 2202 of the second adsorption runner 220. The second cooling gas inlet line 222 is for fresh air or outside air to enter (as shown in FIG. 5), and provides cooling temperature 2202 of the second adsorption runner 220 through the fresh air or outside air for cooling. In another second embodiment, the second clean air discharge line 221 is provided with a second clean air communication line 283, and the other end of the second clean air communication line 283 is connected to the second cooling air intake The pipeline 222 is connected (as shown in FIG. 6) so that the gas in the second clean gas discharge line 221 can be sent to the second adsorption runner 220 for cooling through the second clean gas communication line 283 The area 2202 is used for cooling, and the second clean air communication line 283 is provided with a second clean air communication control valve 2831 (as shown in FIG. 6) to control the air volume of the second clean air communication line 283 .

另該一第二脫附濃縮氣體管路225的一端係與該第二吸附轉輪220之脫附區2203的另一側B連接，而該第二脫附濃縮氣體管路225的另一端係與一焚燒裝置200連接(如第5圖及第6圖所示)，其中該焚燒裝置200係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第二種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置200乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置200不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置2 00為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口201及出口202，而該入口201係與該第二脫附濃縮氣體管路225連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第二脫附濃縮氣體管路225來輸送到該蓄熱式焚燒爐(RTO)之入口201，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口202則連接至該煙囪270(如第5圖及第6圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪270來排出，另該第二脫附濃縮氣體管路225係設有一風機2251，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口201內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the second desorption concentrated gas line 225 is connected to the other side B of the desorption zone 2203 of the second adsorption runner 220, and the other end of the second desorption concentrated gas line 225 is Connected to an incinerator 200 (as shown in Figures 5 and 6), where the incinerator 200 is a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or heat storage One of the two types of incinerators (RTO), and the diagram of the second implementation structure of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 200 described below is a regenerative incinerator (RTO) ), but the incinerator 200 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). And when the incinerator 2 When 00 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 201 and an outlet 202, and the inlet 201 is connected to the second desorbed concentrated gas pipeline 225 so that it can pass through The desorbed concentrated gas desorbed by the high temperature is delivered to the inlet 201 of the regenerative incinerator (RTO) through the second desorbed concentrated gas pipeline 225, so that the desorbed concentrated gas can enter the regenerative incinerator (RTO) ) To carry out high temperature cracking in order to reduce volatile organic compounds, and the outlet 202 of the regenerative incinerator (RTO) is connected to the chimney 270 (as shown in Figures 5 and 6), so as to undergo high temperature cracking The clean gas after the organic matter can be discharged through the chimney 270, and the second desorption concentrated gas pipeline 225 is provided with a fan 2251 to push and pull the desorbed concentrated gas into the inlet of the regenerative incinerator (RTO) In 201, the desorbed concentrated gas can be cracked at high temperature.

而本發明第二種實施架構(如第5圖及第6圖所示)中主要在於該第二吸附轉輪220除了設有吸附區2201、冷卻區2202及脫附區2203外，還設有高溫脫附區2204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪220能恢復其吸附能力，使該第二吸附轉輪220能具有四個區域。而該第二吸附轉輪220之高溫脫附區2204的一側A係與一第四熱氣輸送管路226的一端連接，且該第四熱氣輸送管路226的另一端係與該第四加熱裝置260連接(如第5圖及第6圖所示)，其中該第四加熱裝置260係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第三熱氣輸送管路224係設有一第三熱氣旁通管路292，該第三熱氣旁通管路292的另一端 係與該第四加熱裝置260連接(如第5圖及第6圖所示)，以能將經由該第三加熱裝置250進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路292來輸送到該第四加熱裝置260內，以將進入該第四熱氣輸送管路226內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路226內的高溫熱氣再輸送到該第二吸附轉輪220之高溫脫附區2204，以供進行高溫脫附使用，另該第三熱氣旁通管路292係設有一第三熱氣旁通控制閥門2921(如第6圖所示)，以控制該第三熱氣旁通管路292的風量。 The second implementation structure of the present invention (as shown in FIG. 5 and FIG. 6) mainly lies in that the second adsorption rotor 220 is provided with an adsorption zone 2201, a cooling zone 2202 and a desorption zone 2203, The high-temperature desorption zone 2204 can be used to remove residual high-boiling organic compounds (VOC) during online operation (ON LINE), so that the second adsorption runner 220 can restore its adsorption capacity to enable the second adsorption The runner 220 can have four areas. One side A of the high temperature desorption zone 2204 of the second adsorption runner 220 is connected to one end of a fourth hot gas delivery line 226, and the other end of the fourth hot gas delivery line 226 is connected to the fourth heating The device 260 is connected (as shown in FIGS. 5 and 6), wherein the fourth heating device 260 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is Any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown in the figure) is any one using gas fuel or liquid fuel. The third hot gas delivery line 224 is provided with a third hot gas bypass line 292, and the other end of the third hot gas bypass line 292 It is connected to the fourth heating device 260 (as shown in FIG. 5 and FIG. 6), so that the high-temperature hot gas that is heated or heat-exchanged by the third heating device 250 can be partially shunted through the third hot gas Bypassing the pipeline 292 to the fourth heating device 260 to raise the high-temperature hot gas entering the fourth hot gas transportation line 226 to a certain temperature (for example, 300°C), and transferring the fourth hot gas transportation line The high-temperature hot gas in 226 is sent to the high-temperature desorption area 2204 of the second adsorption runner 220 for high-temperature desorption, and the third hot-gas bypass line 292 is provided with a third hot-gas bypass control valve 2921 (as shown in Figure 6) to control the air volume of the third hot gas bypass line 292.

再者，該第二吸附轉輪220之高溫脫附區2204的另一側B係連接一第二高溫脫附濃縮氣體管路227(如第5圖及第6圖所示)，而該第二高溫脫附濃縮氣體管路227的另一端係與該第二脫附濃縮氣體管路225連接，以將經過該第二吸附轉輪220之高溫脫附區2204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路227來輸送到該第二脫附濃縮氣體管路225內，再透過該第二脫附濃縮氣體管路225輸送到該蓄熱式焚燒爐(RTO)之入口201，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路225內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, the other side B of the high-temperature desorption zone 2204 of the second adsorption runner 220 is connected to a second high-temperature desorption concentrated gas pipeline 227 (as shown in FIGS. 5 and 6), and the first The other end of the two high-temperature desorption concentrated gas pipelines 227 is connected to the second desorption concentrated gas pipeline 225 to desorb the high-temperature desorbed through the high-temperature desorption zone 2204 of the second adsorption runner 220 The concentrated gas can be transported into the second desorption concentrated gas line 225 through the second high-temperature desorption concentrated gas line 227, and then transferred to the regenerative incinerator through the second desorption concentrated gas line 225 ( The inlet 201 of the RTO) allows the high-temperature desorption concentrated gas to enter the regenerative incinerator (RTO) together with the desorption concentrated gas in the second desorption concentrated gas line 225 for high-temperature cracking.

另本發明第三種實施方式的具高溫脫附之轉輪方法，主要係設有一第一吸附轉輪310、一第二吸附轉輪320、一第一加熱裝置330、一第二加熱裝置340、一第三加熱裝置350及一第四加熱裝置360，而該第一吸附轉輪310係設有吸附區3101、冷卻區3102、脫附區3103及高溫脫附區3104，另該第二吸附轉輪320係 設有吸附區3201、冷卻區3202、脫附區3203及高溫脫附區3204，因此，本發明主要在於該第一吸附轉輪310及該第二吸附轉輪320除了設有吸附區3101、3201、冷卻區3102、3202及脫附區3103、3203外，還設有高溫脫附區3104、3204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪310及該第二吸附轉輪320能恢復其吸附能力，使該第一吸附轉輪310及該第二吸附轉輪320能具有四個區域。 In addition, in the third embodiment of the present invention, the runner method with high temperature desorption mainly includes a first adsorption runner 310, a second adsorption runner 320, a first heating device 330, and a second heating device 340 , A third heating device 350 and a fourth heating device 360, and the first adsorption runner 310 is provided with an adsorption zone 3101, a cooling zone 3102, a desorption zone 3103 and a high-temperature desorption zone 3104, and the second adsorption Runner 320 series An adsorption zone 3201, a cooling zone 3202, a desorption zone 3203, and a high-temperature desorption zone 3204 are provided. Therefore, the present invention mainly lies in that the first adsorption runner 310 and the second adsorption runner 320 are provided with adsorption zones 3101, 3201 , Cooling zone 3102, 3202 and desorption zone 3103, 3203, there are also high-temperature desorption zone 3104, 3204, for online operation (ON LINE), the residual high boiling point organic matter (VOC) can be removed , So that the first adsorption runner 310 and the second adsorption runner 320 can restore their adsorption capabilities, so that the first adsorption runner 310 and the second adsorption runner 320 can have four regions.

而該第三種實施方式的主要步驟(如第7圖所示)係包括：步驟S300輸入待吸附之氣體：該第一吸附轉輪310之吸附區3101的一側A係由一廢氣進氣管路311來輸入待吸附之氣體，而該第一吸附轉輪310之吸附區3101的另一側B則透過一第一淨氣排放管路312來輸送經過吸附後之氣體；透過該第一吸附轉輪310之吸附區3101的一側A係連接一廢氣進氣管路311(如第8圖及第9圖所示)，以能由該廢氣進氣管路311來輸入待吸附之氣體，而該待吸附之氣體可以為揮發性有機化合物(VOC)、二氧化碳(CO2)、氮氣(N2)、水氣或氧氣(O2)之其中任一或複數組合之一，也可以是其他上述未表述之氣體，而該第一吸附轉輪310之吸附區3101的另一側B則與該一第一淨氣排放管路312之一端連接(如第8圖及第9圖所示)，讓該待吸附之氣體經該第一吸附轉輪310之吸附區3101進行吸附後再由該第一淨氣排放管路312來輸送經過吸附後之氣體。而完成上述步驟S300後即進行下一步驟S310。 The main steps of the third embodiment (as shown in FIG. 7) include: Step S300: Input gas to be adsorbed: Side A of the adsorption zone 3101 of the first adsorption runner 310 is fed by an exhaust gas The pipeline 311 is used to input the gas to be adsorbed, and the other side B of the adsorption area 3101 of the first adsorption runner 310 is used to convey the adsorbed gas through a first clean gas discharge line 312; One side A of the adsorption zone 3101 of the adsorption rotor 310 is connected to an exhaust gas intake line 311 (as shown in FIGS. 8 and 9 ), so that the exhaust gas intake line 311 can input the gas to be adsorbed The gas to be adsorbed can be any one or a combination of volatile organic compounds (VOC), carbon dioxide (CO2), nitrogen (N2), water vapor or oxygen (O2), or other combinations of the above Expressed gas, and the other side B of the adsorption zone 3101 of the first adsorption runner 310 is connected to one end of the first clean gas discharge line 312 (as shown in FIGS. 8 and 9), let The gas to be adsorbed is adsorbed by the adsorption zone 3101 of the first adsorption runner 310, and then the adsorbed gas is transported by the first clean gas discharge line 312. After the above step S300 is completed, the next step S310 is performed.

另，下一步進行的步驟S310輸入用來冷卻之氣體：該第 一吸附轉輪310之冷卻區3102的一側A係由一第一冷卻氣進氣管路313來輸入用來冷卻之氣體，而該第一吸附轉輪310之冷卻區3102的另一側B則透過一第一冷卻氣輸送管路314來連接至該第一加熱裝置330，以將經過該第一吸附轉輪310之冷卻區3102的氣體輸送到該第一加熱裝置330內；該第一吸附轉輪310之冷卻區3102的一側A係連接一第一冷卻氣進氣管路313(如第8圖及第9圖所示)，以供用來冷卻之氣體進入該第一吸附轉輪310之冷卻區3102來進行冷卻使用，而該第一吸附轉輪310之冷卻區3102的另一側B則連接一第一冷卻氣輸送管路314(如第8圖及第9圖所示)，該第一冷卻氣輸送管路314的另一端係與該第一加熱裝置330連接，使能將經過該第一吸附轉輪310之冷卻區3102的氣體輸送到該第一加熱裝置330內。 In addition, in the next step S310, enter the gas used for cooling: the first One side A of the cooling zone 3102 of an adsorption runner 310 is supplied with gas for cooling by a first cooling air intake line 313, and the other side B of the cooling zone 3102 of the first adsorption runner 310 Connected to the first heating device 330 through a first cooling gas delivery line 314 to deliver the gas passing through the cooling zone 3102 of the first adsorption runner 310 to the first heating device 330; the first A side A of the cooling zone 3102 of the adsorption runner 310 is connected to a first cooling gas intake line 313 (as shown in FIGS. 8 and 9) for the gas used for cooling to enter the first adsorption runner The cooling zone 3102 of 310 is used for cooling, and the other side B of the cooling zone 3102 of the first adsorption runner 310 is connected to a first cooling gas delivery line 314 (as shown in FIGS. 8 and 9) The other end of the first cooling gas delivery line 314 is connected to the first heating device 330, enabling the gas passing through the cooling zone 3102 of the first adsorption runner 310 to be transferred into the first heating device 330.

而上述該第一加熱裝置330係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第一吸附轉輪310之冷卻區3102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪310之冷卻區3102的一側A所連接的第一冷卻氣進氣管路313乃是供新鮮空氣或外氣進入(如第8圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪310之冷卻區3102降溫用。另第二種實施態樣係該廢氣進氣管路311係設有一廢氣連通管路381，而該廢氣連通管路381的另一端係與該第一冷卻氣進氣管路313連接(如第9圖所示)，以能透過該廢氣連通管路381 來將該廢氣進氣管路311內的廢氣輸送到該第一吸附轉輪310之冷卻區3102以進行降溫使用，另該廢氣連通管路381係設有一廢氣連通控制閥門3811(如第9圖所示)，以控制該廢氣連通管路381的風量。而完成上述步驟S310後即進行下一步驟S320。 The above-mentioned first heating device 330 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling zone 3102 of the first adsorption runner 310 described above is provided with two implementation forms, wherein the first implementation form is the first connected to one side A of the cooling zone 3102 of the first adsorption runner 310 The cooling gas inlet line 313 is for fresh air or outside air to enter (as shown in FIG. 8 ), and the cooling area 3102 of the first adsorption runner 310 is provided for cooling through the fresh air or outside air. Another second embodiment is that the exhaust gas intake line 311 is provided with an exhaust gas communication line 381, and the other end of the exhaust gas communication line 381 is connected to the first cooling gas intake line 313 (such as 9)) to allow the exhaust gas to communicate with the pipeline 381 The exhaust gas in the exhaust gas inlet line 311 is sent to the cooling zone 3102 of the first adsorption runner 310 for cooling, and the exhaust gas communication line 381 is provided with an exhaust gas communication control valve 3811 (as shown in FIG. 9 Shown) to control the air volume of the exhaust gas communication line 381. After the above step S310 is completed, the next step S320 is performed.

另，下一步進行的步驟S320輸送高溫熱氣進行脫附：該第一吸附轉輪310之脫附區3103的另一側B係由一第一熱氣輸送管路315來輸送該第一加熱裝置330內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路315係設有一第一熱氣旁通管路391，透過該第一熱氣旁通管路391連接至該第二加熱裝置340，而該第一吸附轉輪310之脫附區3103的一側A則透過一第一脫附濃縮氣體管路316來輸送經過脫附後之脫附濃縮氣體；該第一吸附轉輪310之脫附區3103的另一側B係與該一第一熱氣輸送管路315連接，且該第一熱氣輸送管路315的另一端則與該第一加熱裝置330連接(如第8圖及第9圖所示)，以能將經由該第一加熱裝置330進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路315來輸送到該第一吸附轉輪310之脫附區3103來進行脫附使用。另該第一熱氣輸送管路315係設有一第一熱氣旁通管路391，該第一熱氣旁通管路391的另一端係與該第二加熱裝置340連接(如第8圖及第9圖所示)，以能將經由該第一加熱裝置330進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路391來輸送到該第二加熱裝置340內，另該第一吸附轉輪310之脫附區3103的一側A係連接一第一脫附濃縮氣體管路316的一端(如第8圖及第9圖所示)，以用輸送經過該第一吸附轉輪310之脫 附區3103進行脫附後之脫附濃縮氣體。 In addition, the next step S320 transports high-temperature hot gas for desorption: the other side B of the desorption zone 3103 of the first adsorption runner 310 is transported by a first hot gas delivery pipeline 315 to the first heating device 330 The high-temperature hot gas generated therein is used for desorption, and the first hot gas delivery pipeline 315 is provided with a first hot gas bypass pipeline 391, which is connected to the second heating device 340 through the first hot gas bypass pipeline 391 And the side A of the desorption zone 3103 of the first adsorption runner 310 conveys the desorbed concentrated gas after desorption through a first desorption concentrated gas line 316; the first adsorption runner 310 The other side B of the desorption zone 3103 is connected to the first hot gas delivery pipe 315, and the other end of the first hot gas delivery pipe 315 is connected to the first heating device 330 (as shown in FIGS. 8 and (Figure 9), the high-temperature hot gas heated or exchanged by the first heating device 330 can be transported to the desorption zone 3103 of the first adsorption runner 310 through the first hot gas delivery pipe 315 Use for desorption. In addition, the first hot gas delivery line 315 is provided with a first hot gas bypass line 391, and the other end of the first hot gas bypass line 391 is connected to the second heating device 340 (as shown in FIGS. 8 and 9 As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the first heating device 330 can be partially diverted and sent to the second heating device 340 through the first hot gas bypass line 391, and One side A of the desorption zone 3103 of the first adsorption runner 310 is connected to one end of a first desorption concentrated gas pipeline 316 (as shown in FIG. 8 and FIG. 9) for transportation through the first Adsorption runner 310 off The desorption concentrated gas after desorption is carried out in the attachment zone 3103.

而上述該第二加熱裝置340係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該第一熱氣旁通管路391係設有一第一熱氣旁通控制閥門3911(如第9圖所示)，以控制該第一熱氣旁通管路391的風量，使能將經由該第一加熱裝置330進行加熱或熱交換的高溫熱氣部分分流到該第二加熱裝置340內。而完成上述步驟S320後即進行下一步驟S330。 The above-mentioned second heating device 340 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. And the first hot gas bypass line 391 is provided with a first hot gas bypass control valve 3911 (as shown in FIG. 9) to control the air volume of the first hot gas bypass line 391, so that The high-temperature hot gas that is heated or exchanged by the first heating device 330 is partially shunted into the second heating device 340. After the above step S320 is completed, the next step S330 is performed.

另，下一步進行的步驟S330再將高沸點有機物脫出：該第一吸附轉輪310之高溫脫附區3104的另一側B係由一第二熱氣輸送管路317來輸送由該第二加熱裝置340內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪310之高溫脫附區3104的一側A則透過一第一高溫脫附濃縮氣體管路318來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路316內；該第一吸附轉輪310之高溫脫附區3104的另一側B係與一第二熱氣輸送管路317的一端連接，且該第二熱氣輸送管路317的另一端係與該第二加熱裝置340連接(如第8圖及第9圖所示)，透過該第二加熱裝置340來將進入該第二熱氣輸送管路317內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路317內的高溫熱氣再輸送到該第一吸附轉輪310之高溫脫附區3104，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第 一吸附轉輪310能恢復其吸附能力，另該第一吸附轉輪310之高溫脫附區3104的一側A係連接一第一高溫脫附濃縮氣體管路318(如第8圖及第9圖所示)，而該第一高溫脫附濃縮氣體管路318的另一端係與該第一脫附濃縮氣體管路316連接，以將經過該第一吸附轉輪310之高溫脫附區3104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路318來輸送到該第一脫附濃縮氣體管路316內。 In addition, in the next step S330, high-boiling organics are removed again: the other side B of the high-temperature desorption zone 3104 of the first adsorption runner 310 is conveyed by a second hot gas conveying pipeline 317 by the second The high-temperature hot gas raised to a certain temperature in the heating device 340 to remove high-boiling point organic compounds (VOC), and the side A of the high-temperature desorption zone 3104 of the first adsorption runner 310 passes through a first high-temperature desorption The concentrated gas pipeline 318 is used to transport the desorbed concentrated gas after high temperature to the first desorbed concentrated gas pipeline 316; the other side B of the high temperature desorption zone 3104 of the first adsorption runner 310 is One end of a second hot gas delivery pipe 317 is connected, and the other end of the second hot gas delivery pipe 317 is connected to the second heating device 340 (as shown in FIGS. 8 and 9), through the second The heating device 340 can raise the high-temperature hot gas entering the second hot gas delivery pipe 317 to a certain temperature (for example, 300°C), and then deliver the high-temperature hot gas in the second hot gas delivery pipe 317 to the first adsorption rotor The high-temperature desorption zone 3104 of the wheel 310 is used for high-temperature desorption. When online operation (ON LINE), the residual high-boiling organic matter (VOC) can be removed, so that the first An adsorption runner 310 can restore its adsorption capacity, and another side A of the high temperature desorption zone 3104 of the first adsorption runner 310 is connected to a first high temperature desorption concentrated gas line 318 (as shown in FIGS. 8 and 9 (Shown), and the other end of the first high temperature desorption concentrated gas line 318 is connected to the first desorption concentrated gas line 316 to pass through the high temperature desorption zone 3104 of the first adsorption runner 310 The desorbed high-temperature desorption concentrated gas can be transported into the first desorption concentrated gas line 316 through the first high-temperature desorption concentrated gas line 318.

而上述該第一脫附濃縮氣體管路316的另一端係與一焚燒裝置300連接(如第8圖及第9圖所示)，其中該焚燒裝置300係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第三種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置300乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置300不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置300為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口301及出口302，而該入口301係與該第一脫附濃縮氣體管路316連接，其中該第一脫附濃縮氣體管路316另有與該第一高溫脫附濃縮氣體管路318的另一端連接，以將經過該第一吸附轉輪310之高溫脫附區3104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路318來輸送到該第一脫附濃縮氣體管路316內，使該第一脫附濃縮氣體管路316內除了經過該第一吸附轉輪310之脫附區3103所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路316內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行 高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口302則連接至一煙囪370(如第8圖及第9圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪370來排出，另該第一脫附濃縮氣體管路316係設有一風機3161(如第9圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口301內，讓脫附濃縮氣體能進行高溫裂解。而完成上述步驟S330後即進行下一步驟S340。 The other end of the first desorption concentrated gas pipeline 316 is connected to an incinerator 300 (as shown in FIGS. 8 and 9), wherein the incinerator 300 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown), or regenerative incinerator (RTO), and the illustration of the third embodiment of the present invention takes the regenerative incinerator (RTO) as an example, Moreover, the incinerator 300 described below is a regenerative incinerator (RTO), but the incinerator 300 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (FIG. Not shown) or catalyst furnace (not shown). When the incinerator 300 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 301 and an outlet 302, and the inlet 301 is connected to the first desorption concentrated gas pipeline 316 , Wherein the first desorption concentrated gas pipeline 316 is additionally connected to the other end of the first high-temperature desorption concentrated gas pipeline 318 to desorb the high-temperature desorption zone 3104 passing through the first adsorption runner 310 The lower high-temperature desorption concentrated gas can be transported into the first desorption concentrated gas line 316 through the first high-temperature desorption concentrated gas line 318, so that the first desorption concentrated gas line 316 passes through the The desorption concentrated gas desorbed by the desorption zone 3103 of the first adsorption runner 310 also contains high-temperature desorption concentrated gas, so that the high-temperature desorption concentrated gas can be desorbed from the first desorption concentrated gas pipeline 316 With concentrated gas, enter the regenerative incinerator (RTO) High-temperature cracking to reduce volatile organic compounds, and the outlet 302 of the regenerative incinerator (RTO) is connected to a chimney 370 (as shown in Figures 8 and 9) to crack organic compounds after high-temperature cracking The clean gas can be discharged by the chimney 370, and the first desorption concentrated gas pipeline 316 is provided with a fan 3161 (as shown in FIG. 9) to push and pull the desorbed concentrated gas into the regenerative incineration The inlet 301 of the furnace (RTO) allows the desorbed concentrated gas to undergo high-temperature cracking. After the above step S330 is completed, the next step S340 is performed.

另，下一步進行的步驟S340輸送欲再吸附之氣體：該第二吸附轉輪320之吸附區3201的一側A係由該第一淨氣排放管路312來輸送欲進行再吸附之氣體，而該第二吸附轉輪320之吸附區3201的另一側B則透過一第二淨氣排放管路321來輸送經過再吸附後之氣體；該第二吸附轉輪320之吸附區3201的一側A係與該第一淨氣排放管路312的另一端相連接(如第8圖及第9圖所示)，使該第一淨氣排放管路312內經過吸附後之氣體能直接再輸送到該第二吸附轉輪320之吸附區3201內進行再吸附，另該第二吸附轉輪320之吸附區3201的另一側B係連接一第二淨氣排放管路321，並透過該第二淨氣排放管路321來輸送經過再吸附後之氣體。 In addition, the next step S340 is to transport the gas to be re-adsorbed: the side A of the adsorption area 3201 of the second adsorption rotor 320 is to transport the gas to be re-adsorbed by the first clean gas discharge line 312, The other side B of the adsorption zone 3201 of the second adsorption runner 320 conveys the re-adsorbed gas through a second clean gas discharge line 321; one of the adsorption zones 3201 of the second adsorption runner 320 Side A is connected to the other end of the first clean gas discharge line 312 (as shown in FIGS. 8 and 9), so that the adsorbed gas in the first clean gas discharge line 312 can be directly recycled It is sent to the adsorption zone 3201 of the second adsorption runner 320 for re-adsorption, and the other side B of the adsorption zone 3201 of the second adsorption runner 320 is connected to a second clean gas discharge line 321 and passes through the The second clean gas discharge line 321 conveys the gas after re-adsorption.

而上述該第二淨氣排放管路321之另一端則與一煙囪370連接(如第8圖及第9圖所示)，以方便將經由該第一吸附轉輪310之吸附區3101及該第二吸附轉輪320之吸附區3201所吸附過後之氣體透過該煙囪370來進行排放，其中該第二淨氣排放管路321係設有一風機3211(如第9圖所示)，以增加氣體之流速來流向該煙囪370。而完成上述步驟S340後即進行下一步驟S350。 The other end of the second clean gas discharge pipe 321 is connected to a chimney 370 (as shown in FIGS. 8 and 9 ), so as to facilitate the adsorption zone 3101 passing through the first adsorption runner 310 and the The gas adsorbed by the adsorption zone 3201 of the second adsorption runner 320 is discharged through the chimney 370, wherein the second clean gas discharge line 321 is provided with a fan 3211 (as shown in FIG. 9) to increase the gas The flow velocity comes to the chimney 370. After the above step S340 is completed, the next step S350 is performed.

另，下一步進行的步驟S350輸入用來冷卻之氣體：該第二吸附轉輪320之冷卻區3202的另一側B係由一第二冷卻氣進氣管路322來輸入用來冷卻之氣體，而該第二吸附轉輪320之冷卻區3202的一側A則透過一第二冷卻氣輸送管路323來連接至該第三加熱裝置350，以將經過該第二吸附轉輪320之冷卻區3202的氣體輸送到該第三加熱裝置350內；該第二吸附轉輪320之冷卻區3202的另一側B係連接一第二冷卻氣進氣管路322(如第8圖及第9圖所示)，以供用來冷卻之氣體進入該第二吸附轉輪320之冷卻區3202來進行冷卻使用，而該第二吸附轉輪320之冷卻區3202的一側A則連接一第二冷卻氣輸送管路323(如第8圖及第9圖所示)，該第二冷卻氣輸送管路323的另一端係與該第三加熱裝置350連接，使能將經過該第二吸附轉輪320之冷卻區3202的氣體輸送到該第三加熱裝置350內。 In addition, in the next step S350, the gas used for cooling is input: the other side B of the cooling zone 3202 of the second adsorption runner 320 is fed with a gas for cooling by a second cooling gas inlet line 322 , And the side A of the cooling zone 3202 of the second adsorption runner 320 is connected to the third heating device 350 through a second cooling gas delivery line 323 to cool the passing of the second adsorption runner 320 The gas in zone 3202 is delivered to the third heating device 350; the other side B of the cooling zone 3202 of the second adsorption runner 320 is connected to a second cooling gas inlet line 322 (as shown in Figures 8 and 9 As shown in the figure), the gas used for cooling enters the cooling zone 3202 of the second adsorption runner 320 for cooling, and a side A of the cooling zone 3202 of the second adsorption runner 320 is connected to a second cooling The gas conveying pipeline 323 (as shown in FIGS. 8 and 9), the other end of the second cooling gas conveying pipeline 323 is connected to the third heating device 350, enabling the second adsorption runner to pass The gas in the cooling zone 3202 of 320 is delivered into the third heating device 350.

而上述該第三加熱裝置350係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第二吸附轉輪320之冷卻區3202係設有兩種實施態樣，其中第一種實施態樣為該第二吸附轉輪之320冷卻區3202的另一側B所連接的第二冷卻氣進氣管路322乃是供新鮮空氣或外氣進入(如第8圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪320之冷卻區3202降溫用。另第二種實施態樣係該第二淨氣排放管路321係設有一第二淨氣連通管路383，而該第二淨氣連通管路383的另一 端係與該第二冷卻氣進氣管路322連接(如第9圖所示)，以能透過該第二淨氣連通管路383來將該第二淨氣排放管路321內的氣體輸送到該第二吸附轉輪320之冷卻區3202以進行降溫使用，另該第二淨氣連通管路383係設有一第二淨氣連通控制閥門3831(如第9圖所示)，以控制該第二淨氣連通管路383的風量。而完成上述步驟S350後即進行下一步驟S360。 The above-mentioned third heating device 350 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling zone 3202 of the second adsorption runner 320 is provided with two implementation forms, of which the first implementation form is the third section connected to the other side B of the cooling zone 3202 of the second adsorption runner 320. The second cooling gas inlet line 322 is for fresh air or outside air to enter (as shown in FIG. 8), and provides cooling temperature 3202 of the second adsorption runner 320 through the fresh air or outside air for cooling. Another second embodiment is that the second clean air discharge line 321 is provided with a second clean air communication line 383, and the second clean air communication line 383 has another The end system is connected to the second cooling gas intake line 322 (as shown in FIG. 9), so that the gas in the second clean gas discharge line 321 can be transported through the second clean gas communication line 383 To the cooling zone 3202 of the second adsorption runner 320 for cooling, and the second clean gas communication line 383 is provided with a second clean gas communication control valve 3831 (as shown in FIG. 9) to control the The second clean air communicates with the air volume of the pipeline 383. After the above step S350 is completed, the next step S360 is performed.

另，下一步進行的步驟S360輸送高溫熱氣進行脫附：該第二吸附轉輪320之脫附區3203的一側A係由一第三熱氣輸送管路324來輸送該第三加熱裝置350內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路324係設有一第三熱氣旁通管路392，透過該第三熱氣旁通管路392連接至該第四加熱裝置360，而該第二吸附轉輪320之脫附區3203的另一側B則透過一第二脫附濃縮氣體管路325來輸送經過脫附後之脫附濃縮氣體；該第二吸附轉輪320之脫附區3203的一側A係與該一第三熱氣輸送管路324連接，且該第三熱氣輸送管路324的另一端則與該第三加熱裝置350連接(如第8圖及第9圖所示)，以能將經由該第三加熱裝置350進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路324來輸送到該第二吸附轉輪320之脫附區3203來進行脫附使用。另該第三熱氣輸送管路324係設有一第三熱氣旁通管路392(如第8圖及第9圖所示)，該第三熱氣旁通管路392的另一端係與該第四加熱裝置360連接，以能將經由該第三加熱裝置350進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路392來輸送到該第四加熱裝置360內，另該第二吸附轉輪320 之脫附區3203的另一側B係連接一第二脫附濃縮氣體管路325的一端(如第8圖及第9圖所示)，以用輸送經過該第二吸附轉輪320之脫附區3203進行脫附後之脫附濃縮氣體。 In addition, the next step S360 is to transport high-temperature hot gas for desorption: the side A of the desorption zone 3203 of the second adsorption runner 320 is transported into the third heating device 350 by a third hot gas delivery pipeline 324 The generated high-temperature hot gas is used for desorption, and the third hot gas delivery pipeline 324 is provided with a third hot gas bypass pipeline 392, which is connected to the fourth heating device 360 through the third hot gas bypass pipeline 392. The other side B of the desorption zone 3203 of the second adsorption runner 320 conveys the desorbed concentrated gas after desorption through a second desorption concentrated gas line 325; One side A of the desorption zone 3203 is connected to the third hot gas delivery pipe 324, and the other end of the third hot gas delivery pipe 324 is connected to the third heating device 350 (as shown in FIGS. 8 and 9 (Shown), the high-temperature hot gas heated or exchanged by the third heating device 350 can be transported to the desorption area 3203 of the second adsorption runner 320 through the third hot gas delivery pipe 324 for desorption Attached to use. In addition, the third hot gas delivery line 324 is provided with a third hot gas bypass line 392 (as shown in FIGS. 8 and 9 ). The other end of the third hot gas bypass line 392 is connected to the fourth The heating device 360 is connected so that the high-temperature hot gas that is heated or exchanged through the third heating device 350 can be partially shunted, and is transferred to the fourth heating device 360 through the third hot gas bypass line 392, and The second adsorption runner 320 The other side B of the desorption zone 3203 is connected to one end of a second desorption concentrated gas line 325 (as shown in FIG. 8 and FIG. 9) to be transported through the second adsorption runner 320 for desorption The attached area 3203 is desorbed and concentrated gas after desorption.

而上述該第四加熱裝置360係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該第三熱氣旁通管路392係設有一第三熱氣旁通控制閥門3921(如第9圖所示)，以控制該第三熱氣旁通管路392的風量，使能將經由該第三加熱裝置350進行加熱或熱交換的高溫熱氣部分分流到該第四加熱裝置360內。而完成上述步驟S360後即進行下一步驟S370。 The above-mentioned fourth heating device 360 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. And the third hot gas bypass line 392 is provided with a third hot gas bypass control valve 3921 (as shown in FIG. 9) to control the air volume of the third hot gas bypass line 392, enabling The high-temperature hot gas that is heated or exchanged by the third heating device 350 is partially shunted into the fourth heating device 360. After the above step S360 is completed, the next step S370 is performed.

另，下一步進行的步驟S370再將高沸點有機物脫出：該第二吸附轉輪320之高溫脫附區3204的一側A係由一第四熱氣輸送管路326來輸送由該第四加熱裝置360內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪320之高溫脫附區3204的另一側B則透過一第二高溫脫附濃縮氣體管路327來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路325內；該第二吸附轉輪320之高溫脫附區3204的一側A係與一第四熱氣輸送管路326的一端連接，且該第四熱氣輸送管路326的另一端係與該第四加熱裝置360連接(如第8圖及第9圖所示)，透過該第四加熱裝置360來將進入該第四熱氣輸送管路326內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路326內的高溫熱氣再輸送到該第二 吸附轉輪320之高溫脫附區3204，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪320能恢復其吸附能力，另該第二吸附轉輪320之高溫脫附區3204的另一側B係連接一第二高溫脫附濃縮氣體管路327(如第8圖及第9圖所示)，而該第二高溫脫附濃縮氣體管路327的另一端係與該第二脫附濃縮氣體管路325連接，以將經過該第二吸附轉輪320之高溫脫附區3204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路327來輸送到該第二脫附濃縮氣體管路325內。 In addition, in the next step S370, the high-boiling organic matter is removed again: the side A of the high-temperature desorption zone 3204 of the second adsorption runner 320 is conveyed by a fourth hot gas conveying line 326 by the fourth heating The high temperature hot gas raised to a certain temperature in the device 360 to remove high boiling point organic compounds (VOC), and the other side B of the high temperature desorption zone 3204 of the second adsorption runner 320 is desorbed through a second high temperature The concentrated gas pipeline 327 is used to transport the high-temperature desorbed concentrated gas after desorption to the second desorbed concentrated gas pipeline 325; the side A of the high-temperature desorption zone 3204 of the second adsorption runner 320 is connected to a One end of the fourth hot gas delivery line 326 is connected, and the other end of the fourth hot gas delivery line 326 is connected to the fourth heating device 360 (as shown in FIGS. 8 and 9), through which the fourth heating The device 360 raises the high-temperature hot gas entering the fourth hot gas delivery line 326 to a certain temperature (for example, 300°C), and then delivers the high-temperature hot gas in the fourth hot gas delivery line 326 to the second The high-temperature desorption zone 3204 of the adsorption rotor 320 is used for high-temperature desorption. When online operation (ON LINE), the remaining high-boiling organic matter (VOC) can be removed, so that the second adsorption rotor 320 It can restore its adsorption capacity. In addition, the other side B of the high temperature desorption zone 3204 of the second adsorption runner 320 is connected to a second high temperature desorption concentrated gas pipeline 327 (as shown in FIGS. 8 and 9) , And the other end of the second high temperature desorption concentrated gas line 327 is connected to the second desorption concentrated gas line 325 to desorb the high temperature desorption area 3204 passing through the second adsorption runner 320 The high-temperature desorption concentrated gas can be transported into the second desorption concentrated gas line 325 through the second high-temperature desorption concentrated gas line 327.

而上述該第二脫附濃縮氣體管路325的另一端係與一焚燒裝置300連接(如第8圖及第9圖所示)，其中該焚燒裝置300係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第三種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置300乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置300不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置300為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口301及出口302，而該入口301係與該第二脫附濃縮氣體管路325連接，其中該第二脫附濃縮氣體管路325另有與該第二高溫脫附濃縮氣體管路327的另一端連接，以將經過該第二吸附轉輪320之高溫脫附區3204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路327來輸送到該第二脫附濃縮氣體管路325內，使該第二脫附濃縮氣體管路325內除了經過該第二吸附轉輪320之脫附區3203所脫附下來的脫附濃縮氣 體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路325內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口302則連接至一煙囪370(如第8圖及第9圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪370來排出，另該第二脫附濃縮氣體管路325係設有一風機3251(如第9圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口301內，讓脫附濃縮氣體能進行高溫裂解。 The other end of the second desorbed concentrated gas pipeline 325 is connected to an incinerator 300 (as shown in FIGS. 8 and 9), wherein the incinerator 300 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown), or regenerative incinerator (RTO), and the illustration of the third embodiment of the present invention takes the regenerative incinerator (RTO) as an example, Moreover, the incinerator 300 described below is a regenerative incinerator (RTO), but the incinerator 300 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (FIG. Not shown) or catalyst furnace (not shown). When the incinerator 300 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 301 and an outlet 302, and the inlet 301 is connected to the second desorption concentrated gas pipeline 325 , Wherein the second desorption concentrated gas pipeline 325 is additionally connected to the other end of the second high-temperature desorption concentrated gas pipeline 327 to desorb the high-temperature desorption zone 3204 passing through the second adsorption runner 320 The lower high-temperature desorption concentrated gas can be transported into the second desorption concentrated gas line 325 through the second high-temperature desorption concentrated gas line 327, so that the second desorption concentrated gas line 325 passes through the The desorbed concentrated gas desorbed from the desorption area 3203 of the second adsorption runner 320 The body also contains high-temperature desorption concentrated gas, so that the high-temperature desorption concentrated gas can enter the regenerative incinerator (RTO) together with the desorption concentrated gas in the second desorption concentrated gas pipeline 325 for high-temperature cracking to To reduce volatile organic compounds, the outlet 302 of the regenerative incinerator (RTO) is connected to a chimney 370 (as shown in Figure 8 and Figure 9), so that the clean gas after high temperature cracking of organic compounds can The chimney 370 is discharged, and the second desorption concentrated gas pipeline 325 is provided with a fan 3251 (as shown in FIG. 9) to push and pull the desorbed concentrated gas into the regenerative incinerator (RTO) In the inlet 301, the desorbed concentrated gas can be pyrolyzed.

另本發明第三種實施架構的具高溫脫附之轉輪系統(如第8圖及第9圖所示)，主要係透過一第一吸附轉輪310、一第二吸附轉輪320、一第一加熱裝置330、一第二加熱裝置340、一第三加熱裝置350及一第四加熱裝置360之組合設計，而本發明第三種實施架構的第一吸附轉輪310係設有吸附區3101、冷卻區3102、脫附區3103及高溫脫附區3104，該第一吸附轉輪310係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且一廢氣進氣管路311係連接至該第一吸附轉輪310之吸附區3101的一側A(如第8圖及第9圖所示)，以使該第一吸附轉輪310之吸附區3101能吸附該廢氣進氣管路311內的有機物，而該第一吸附轉輪310之吸附區3101的另一側B係與該一第一淨氣排放管路312之一端連接，讓該廢氣經該第一吸附轉輪310之吸附區3101進行吸附有機物後再由該第一淨氣排放管路312來輸送。 In addition, the third embodiment of the present invention is a high-temperature desorption rotor system (as shown in FIGS. 8 and 9), mainly through a first adsorption runner 310, a second adsorption runner 320, a The combined design of the first heating device 330, a second heating device 340, a third heating device 350 and a fourth heating device 360, and the first adsorption runner 310 of the third embodiment of the present invention is provided with an adsorption zone 3101, a cooling zone 3102, a desorption zone 3103, and a high-temperature desorption zone 3104, the first adsorption runner 310 is a zeolite concentration runner or a concentration runner of other materials, and an exhaust gas intake line 311 is connected to One side A (as shown in FIGS. 8 and 9) of the adsorption zone 3101 of the first adsorption runner 310, so that the adsorption zone 3101 of the first adsorption runner 310 can adsorb the exhaust gas intake line 311 Organic matter inside, and the other side B of the adsorption zone 3101 of the first adsorption runner 310 is connected to one end of the first clean gas discharge line 312 to allow the exhaust gas to be adsorbed by the first adsorption runner 310 The area 3101 is transported by the first clean gas discharge line 312 after adsorbing organic matter.

另該第一吸附轉輪310之冷卻區3102的一側A係連 接一第一冷卻氣進氣管路313(如第8圖及第9圖所示)，以供氣體進入該第一吸附轉輪310之冷卻區3102來進行冷卻使用，而該第一吸附轉輪310之冷卻區3102的另一側B係連接一第一冷卻氣輸送管路314(如第8圖及第9圖所示)，該第一冷卻氣輸送管路314的另一端係與該第一加熱裝置330連接，其中該第一加熱裝置330係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第一熱氣輸送管路315的一端係與該第一吸附轉輪310之脫附區3103的另一側B連接(如第8圖及第9圖所示)，且該第一熱氣輸送管路315的另一端則與該第一加熱裝置330連接，以能將經由該第一加熱裝置330進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路315來輸送到該第一吸附轉輪310之脫附區3103來進行脫附使用。 In addition, one side A of the cooling zone 3102 of the first adsorption runner 310 is connected A first cooling gas inlet line 313 (as shown in FIGS. 8 and 9) is provided for the gas to enter the cooling zone 3102 of the first adsorption runner 310 for cooling, and the first adsorption rotor The other side B of the cooling zone 3102 of the wheel 310 is connected to a first cooling gas delivery line 314 (as shown in FIGS. 8 and 9), and the other end of the first cooling gas delivery line 314 is connected to the The first heating device 330 is connected, wherein the first heating device 330 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is an electric heating wire, an electric heating tube or an electric heating sheet In any of them, the pipeline heater (not shown) is any one that uses gas fuel or liquid fuel. One end of the first hot gas delivery pipe 315 is connected to the other side B of the desorption zone 3103 of the first adsorption runner 310 (as shown in FIGS. 8 and 9), and the first hot gas The other end of the conveying pipeline 315 is connected to the first heating device 330 so that high-temperature hot gas heated or exchanged through the first heating device 330 can be conveyed to the first through the first hot gas conveying line 315 The desorption area 3103 of the adsorption rotor 310 is used for desorption.

而上述該第一吸附轉輪310之冷卻區3102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪310之冷卻區3102的一側A所連接的第一冷卻氣進氣管路313乃是供新鮮空氣或外氣進入(如第8圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪310之冷卻區3102降溫用。另第二種實施態樣係該廢氣進氣管路311係設有一廢氣連通管路381，而該廢氣連通管路381的另一端係與該第一冷卻氣進氣管路313連接(如第9圖所示)，以能透過該廢氣連通管路381來將該廢氣進氣管路311內的廢氣輸送到該第一吸附轉輪310之冷卻區3102以進行降溫使用，另該廢氣連通管路381係設有一 廢氣連通控制閥門3811(如第9圖所示)，以控制該廢氣連通管路381的風量。 The cooling zone 3102 of the first adsorption runner 310 is provided with two implementations, of which the first implementation is the first connected to the side A of the cooling zone 3102 of the first adsorption runner 310 The cooling gas inlet line 313 is for fresh air or outside air to enter (as shown in FIG. 8 ), and the cooling area 3102 of the first adsorption runner 310 is provided for cooling through the fresh air or outside air. Another second embodiment is that the exhaust gas intake line 311 is provided with an exhaust gas communication line 381, and the other end of the exhaust gas communication line 381 is connected to the first cooling gas intake line 313 (such as 9)), the exhaust gas in the exhaust gas intake pipe 311 can be transmitted to the cooling zone 3102 of the first adsorption runner 310 through the exhaust gas communication pipe 381 for cooling, and the exhaust gas communication pipe Road 381 has one The exhaust gas communication control valve 3811 (as shown in FIG. 9) controls the air volume of the exhaust gas communication line 381.

另該一第一脫附濃縮氣體管路316的一端係與該第一吸附轉輪310之脫附區3103的一側A連接，而該第一脫附濃縮氣體管路316的另一端係與一焚燒裝置300連接(如第8圖及第9圖所示)，其中該焚燒裝置300係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第三種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置300乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置300不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置300為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口301及出口302，而該入口301係與該第一脫附濃縮氣體管路316連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第一脫附濃縮氣體管路316來輸送到該蓄熱式焚燒爐(RTO)之入口301，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口302則連接至一煙囪370(如第8圖及第9圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪370來排出，另該第一脫附濃縮氣體管路316係設有一風機3161，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口301內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the first desorption concentrated gas line 316 is connected to one side A of the desorption zone 3103 of the first adsorption runner 310, and the other end of the first desorption concentrated gas line 316 is connected to An incinerator 300 is connected (as shown in Figures 8 and 9), where the incinerator 300 is a direct-fired incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative type Any one of the incinerators (RTO), and the illustration of the third implementation structure of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 300 described below is a regenerative incinerator (RTO) However, the incineration device 300 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 300 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 301 and an outlet 302, and the inlet 301 is connected to the first desorption concentrated gas pipeline 316 , So that the desorbed concentrated gas desorbed by high temperature can be transported to the inlet 301 of the regenerative incinerator (RTO) through the first desorbed concentrated gas pipeline 316, so that the desorbed concentrated gas can enter the heat storage Pyrolysis in the incinerator (RTO) to reduce volatile organic compounds, and the outlet 302 of the regenerative incinerator (RTO) is connected to a chimney 370 (as shown in Figures 8 and 9), In order to discharge the clean gas after high-temperature pyrolysis of organic matter through the chimney 370, the first desorption concentrated gas pipeline 316 is provided with a fan 3161 to push and pull the desorbed concentrated gas into the regenerative incinerator (RTO) inlet 301 allows the desorbed concentrated gas to undergo high-temperature cracking.

而本發明第三種實施架構(如第8圖及第9圖所示)中主要在於該第一吸附轉輪310除了設有吸附區3101、冷卻區3102及 脫附區3103外，還設有高溫脫附區3104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪310能恢復其吸附能力，使該第一吸附轉輪310能具有四個區域。而該第一吸附轉輪310之高溫脫附區3104的另一側B係與一第二熱氣輸送管路317的一端連接，且該第二熱氣輸送管路317的另一端係與該第二加熱裝置340連接(如第8圖及第9圖所示)，其中該第二加熱裝置340係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第一熱氣輸送管路315係設有一第一熱氣旁通管路391，該第一熱氣旁通管路391的另一端係與該第二加熱裝置340連接(如第8圖及第9圖所示)，以能將經由該第一加熱裝置330進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路391來輸送到該第二加熱裝置340內，以將進入該第二熱氣輸送管路317內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路317內的高溫熱氣再輸送到該第一吸附轉輪110之高溫脫附區3104，以供進行高溫脫附使用，另該第一熱氣旁通管路391係設有一第一熱氣旁通控制閥門3911(如第9圖所示)，以控制該第一熱氣旁通管路391的風量。 The third implementation structure of the present invention (as shown in FIG. 8 and FIG. 9) mainly lies in that the first adsorption rotor 310 is provided with an adsorption zone 3101, a cooling zone 3102 and In addition to the desorption zone 3103, there is also a high-temperature desorption zone 3104, which can be used to remove the remaining high-boiling organic matter (VOC) during online operation (ON LINE), so that the first adsorption runner 310 can recover Its adsorption capacity enables the first adsorption runner 310 to have four regions. The other side B of the high-temperature desorption zone 3104 of the first adsorption runner 310 is connected to one end of a second hot gas delivery pipe 317, and the other end of the second hot gas delivery pipe 317 is connected to the second The heating device 340 is connected (as shown in Figures 8 and 9), wherein the second heating device 340 is any one of a heater, a pipe heater, or a heat exchanger, and the heater (not shown) is It is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown in the figure) is any one using gas fuel or liquid fuel. The first hot gas delivery line 315 is provided with a first hot gas bypass line 391, and the other end of the first hot gas bypass line 391 is connected to the second heating device 340 (as shown in FIGS. 8 and 9 As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the first heating device 330 can be partially shunted and sent to the second heating device 340 through the first hot gas bypass line 391 to The high-temperature hot gas entering the second hot gas delivery pipe 317 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the second hot gas delivery pipe 317 is then delivered to the high temperature of the first adsorption runner 110 The desorption zone 3104 is used for high temperature desorption. In addition, the first hot gas bypass line 391 is provided with a first hot gas bypass control valve 3911 (as shown in FIG. 9) to control the first hot gas bypass The air volume through the pipeline 391.

再者，該第一吸附轉輪310之高溫脫附區3104的一側A係連接一第一高溫脫附濃縮氣體管路318(如第8圖及第9圖所示)，而該第一高溫脫附濃縮氣體管路318的另一端係與該第一脫附濃縮氣體管路316連接，以將經過該第一吸附轉輪310之高溫脫附區3104 所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路318來輸送到該第一脫附濃縮氣體管路316內，再透過該第一脫附濃縮氣體管路316輸送到該蓄熱式焚燒爐(RTO)之入口301，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路316內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, a side A of the high temperature desorption zone 3104 of the first adsorption runner 310 is connected to a first high temperature desorption concentrated gas line 318 (as shown in FIGS. 8 and 9), and the first The other end of the high-temperature desorption concentrated gas line 318 is connected to the first desorption concentrated gas line 316 to pass through the high-temperature desorption zone 3104 of the first adsorption runner 310 The desorbed high-temperature desorption concentrated gas can be transported into the first desorption concentrated gas line 316 through the first high-temperature desorption concentrated gas line 318, and then through the first desorption concentrated gas line 316 Transported to the inlet 301 of the regenerative incinerator (RTO), so that the high-temperature desorbed concentrated gas can enter the regenerative incinerator (RTO) together with the desorbed concentrated gas in the first desorbed concentrated gas line 316 High temperature cracking.

另該第二吸附轉輪320係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且該第二吸附轉輪320內係設有吸附區3201、冷卻區3202、脫附區3203及高溫脫附區3204，而該第二吸附轉輪320之吸附區3201的一側A係與該第一淨氣排放管路312的另一端相連接(如第8圖及第9圖所示)，使該第一淨氣排放管路312內的氣體能直接再輸送到該第二吸附轉輪320之吸附區3201內進行吸附，另該第二吸附轉輪320之吸附區3201的另一側B係連接一第二淨氣排放管路321，而該第二淨氣排放管路321之另一端則與一煙囪370連接(如第8圖及第9圖所示)，以方便將經由該第一吸附轉輪310之吸附區3101及該第二吸附轉輪320之吸附區3201所吸附過的氣體透過該煙囪370來進行排放，其中該第二淨氣排放管路321係設有一風機3211(如第9圖所示)，以增加氣體之流速來流向該煙囪370。 In addition, the second adsorption runner 320 is a zeolite concentration runner or a concentration runner of other materials, and the second adsorption runner 320 is provided with an adsorption zone 3201, a cooling zone 3202, a desorption zone 3203, and a high temperature desorption Attached area 3204, and one side A of the adsorption area 3201 of the second adsorption rotor 320 is connected to the other end of the first clean gas discharge line 312 (as shown in FIGS. 8 and 9), so that The gas in the first clean gas discharge line 312 can be directly sent to the adsorption area 3201 of the second adsorption rotor 320 for adsorption, and the other side of the adsorption area 3201 of the second adsorption rotor 320 is B A second clean gas discharge line 321 is connected, and the other end of the second clean gas discharge line 321 is connected to a chimney 370 (as shown in FIGS. 8 and 9), so that the first The gas adsorbed by the adsorption zone 3101 of the adsorption runner 310 and the adsorption zone 3201 of the second adsorption runner 320 is discharged through the chimney 370, wherein the second clean gas discharge pipe 321 is provided with a fan 3211 (such as (Shown in Figure 9), the gas flow rate is increased to the chimney 370.

另該第二吸附轉輪320之冷卻區3202的另一側B係連接一第二冷卻氣進氣管路322，以供氣體進入該第二吸附轉輪320之冷卻區3202來進行冷卻使用，而該第二吸附轉輪320之冷卻區3202的一側A係連接一第二冷卻氣輸送管路323(如第8圖及第9圖所示)，該第二冷卻氣輸送管路323的另一端係與該第三加熱裝置350 連接，其中該第三加熱裝置350係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第三熱氣輸送管路324的一端係與該第二吸附轉輪320之脫附區3203的一側A連接，且該第三熱氣輸送管路324的另一端係與該第三加熱裝置350連接(如第8圖及第9圖所示)，以能將經由該第三加熱裝置350進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路324來輸送到該第二吸附轉輪320之脫附區3203來進行脫附使用。 In addition, the other side B of the cooling zone 3202 of the second adsorption runner 320 is connected to a second cooling gas inlet line 322 for the gas to enter the cooling zone 3202 of the second adsorption runner 320 for cooling. A side A of the cooling zone 3202 of the second adsorption runner 320 is connected to a second cooling gas delivery line 323 (as shown in FIGS. 8 and 9 ). The other end is connected to the third heating device 350 Connection, wherein the third heating device 350 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the The pipeline heater (not shown) is either gas fuel or liquid fuel. One end of the third hot gas delivery pipe 324 is connected to one side A of the desorption zone 3203 of the second adsorption rotor 320, and the other end of the third hot gas delivery pipe 324 is connected to the third heating The device 350 is connected (as shown in FIGS. 8 and 9) so that the high-temperature hot gas heated or heat-exchanged by the third heating device 350 can be sent to the second adsorption through the third hot gas delivery line 324 The desorption area 3203 of the runner 320 is used for desorption.

而上述該第二吸附轉輪320之冷卻區3202係設有兩種實施態樣，其中第一種實施態樣為該第二吸附轉輪320之冷卻區3202的另一側B所連接的第二冷卻氣進氣管路322乃是供新鮮空氣或外氣進入(如第8圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪320之冷卻區3202降溫用。另第二種實施方式係該第二淨氣排放管路321係設有一第二淨氣連通管路383，而該第二淨氣連通管路383的另一端係與該第二冷卻氣進氣管路322連接(如第9圖所示)，以能透過該第二淨氣連通管路383來將該第二淨氣排放管路321內的氣體輸送到該第二吸附轉輪320之冷卻區3202以進行降溫使用，另該第二淨氣連通管路383係設有一第二淨氣連通控制閥門3831(如第9圖所示)，以控制該第二淨氣連通管路383的風量。 The cooling zone 3202 of the second adsorption runner 320 is provided with two implementations, of which the first implementation is the connection of the second side B of the cooling zone 3202 of the second adsorption runner 320. The second cooling gas inlet line 322 is for fresh air or outside air to enter (as shown in FIG. 8), and provides cooling temperature 3202 of the second adsorption runner 320 through the fresh air or outside air for cooling. Another second embodiment is that the second clean air discharge line 321 is provided with a second clean air communication line 383, and the other end of the second clean air communication line 383 is connected to the second cooling air intake The pipeline 322 is connected (as shown in FIG. 9) so that the gas in the second clean gas discharge line 321 can be sent to the second adsorption runner 320 for cooling through the second clean gas communication line 383 Zone 3202 is used for cooling. In addition, the second clean air communication line 383 is provided with a second clean air communication control valve 3831 (as shown in FIG. 9) to control the air volume of the second clean air communication line 383 .

另該一第二脫附濃縮氣體管路325的一端係與該第二吸附轉輪320之脫附區3203的另一側B連接，而該第二脫附濃縮氣體管路325的另一端係與一焚燒裝置300連接(如第8圖及第9圖所 示)，其中該焚燒裝置300係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第三種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置300乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置300不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置300為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口301及出口302，而該入口301係與該第二脫附濃縮氣體管路325連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第二脫附濃縮氣體管路325來輸送到該蓄熱式焚燒爐(RTO)之入口301，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口302則連接至該煙囪370(如第8圖及第9圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪370來排出，另該第二脫附濃縮氣體管路325係設有一風機3251，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口301內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the second desorption concentrated gas line 325 is connected to the other side B of the desorption zone 3203 of the second adsorption runner 320, and the other end of the second desorption concentrated gas line 325 is Connected to an incinerator 300 (as shown in Figures 8 and 9 Shown), wherein the incineration device 300 is any one of a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative incinerator (RTO), and the present invention is third The illustration of this kind of implementation architecture takes the regenerative incinerator (RTO) as an example, and the incinerator 300 described below is a regenerative incinerator (RTO), but the incinerator 300 of the present invention does not use a regenerative incinerator ( RTO) is limited, it can also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 300 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 301 and an outlet 302, and the inlet 301 is connected to the second desorption concentrated gas pipeline 325 , So that the desorbed concentrated gas desorbed by high temperature can be transported to the inlet 301 of the regenerative incinerator (RTO) through the second desorbed concentrated gas pipeline 325, so that the desorbed concentrated gas can enter the heat storage High temperature pyrolysis in the incinerator (RTO) to reduce volatile organic compounds, and the outlet 302 of the regenerative incinerator (RTO) is connected to the chimney 370 (as shown in Figures 8 and 9), In order to discharge the clean gas after high-temperature pyrolysis of organic matter through the chimney 370, the second desorption concentrated gas pipeline 325 is provided with a fan 3251 to push and pull the desorbed concentrated gas into the regenerative incinerator (RTO) inlet 301 allows the desorbed concentrated gas to undergo high-temperature cracking.

而本發明第三種實施架構(如第8圖及第9圖所示)中主要在於該第二吸附轉輪320除了設有吸附區3201、冷卻區3202及脫附區3203外，還設有高溫脫附區3204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪320能恢復其吸附能力，使該第二吸附轉輪320能具有四個區域。而該第二吸附轉輪320之高溫脫附區3204的一側A係與一第四熱氣輸送管路326的一端連接，且該第四熱氣輸送管路326的另一端係與該 第四加熱裝置360連接(如第8圖及第9圖所示)，其中該第四加熱裝置360係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第三熱氣輸送管路324係設有一第三熱氣旁通管路392，該第三熱氣旁通管路392的另一端係與該第四加熱裝置360連接(如第8圖及第9圖所示)，以能將經由該第三加熱裝置350進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路392來輸送到該第四加熱裝置360內，以將進入該第四熱氣輸送管路326內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路326內的高溫熱氣再輸送到該第二吸附轉輪320之高溫脫附區3204，以供進行高溫脫附使用，另該第三熱氣旁通管路392係設有一第三熱氣旁通控制閥門3921(如第9圖所示)，以控制該第三熱氣旁通管路392的風量。 The third implementation structure of the present invention (as shown in FIG. 8 and FIG. 9) is mainly that in addition to the adsorption area 3201, the cooling area 3202 and the desorption area 3203, the second adsorption rotor 320 is also provided with The high-temperature desorption zone 3204 can be used to remove residual high-boiling organic compounds (VOC) during on-line operation (ON LINE), so that the second adsorption runner 320 can restore its adsorption capacity, so that the second adsorption The runner 320 can have four areas. One side A of the high-temperature desorption zone 3204 of the second adsorption runner 320 is connected to one end of a fourth hot gas delivery line 326, and the other end of the fourth hot gas delivery line 326 is connected to the The fourth heating device 360 is connected (as shown in FIGS. 8 and 9), wherein the fourth heating device 360 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown in the figure) ) Is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown) is any of gas fuel or liquid fuel. The third hot gas delivery line 324 is provided with a third hot gas bypass line 392, and the other end of the third hot gas bypass line 392 is connected to the fourth heating device 360 (as shown in FIGS. 8 and 9 As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the third heating device 350 can be partially shunted and transported into the fourth heating device 360 through the third hot gas bypass line 392 to The high-temperature hot gas entering the fourth hot gas delivery line 326 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the fourth hot gas delivery line 326 is sent to the high temperature of the second adsorption runner 320 The desorption zone 3204 is used for high temperature desorption, and the third hot gas bypass line 392 is provided with a third hot gas bypass control valve 3921 (as shown in FIG. 9) to control the third hot gas bypass The air volume through the pipeline 392.

再者，該第二吸附轉輪320之高溫脫附區3204的另一側B係連接一第二高溫脫附濃縮氣體管路327(如第8圖及第9圖所示)，而該第二高溫脫附濃縮氣體管路327的另一端係與該第二脫附濃縮氣體管路325連接，以將經過該第二吸附轉輪320之高溫脫附區3204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路327來輸送到該第二脫附濃縮氣體管路325內，再透過該第二脫附濃縮氣體管路325輸送到該蓄熱式焚燒爐(RTO)之入口301，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路325內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, the other side B of the high temperature desorption zone 3204 of the second adsorption runner 320 is connected to a second high temperature desorption concentrated gas line 327 (as shown in FIGS. 8 and 9), and the first The other end of the two high-temperature desorption concentrated gas pipelines 327 is connected to the second desorption concentrated gas pipeline 325 to desorb the high-temperature desorbed through the high-temperature desorption zone 3204 of the second adsorption runner 320 The concentrated gas can be transported into the second desorption concentrated gas line 325 through the second high-temperature desorption concentrated gas line 327, and then transferred to the regenerative incinerator through the second desorption concentrated gas line 325 ( The inlet 301 of the RTO) allows the high-temperature desorption concentrated gas to enter the regenerative incinerator (RTO) together with the desorption concentrated gas in the second desorption concentrated gas line 325 for high-temperature cracking.

另本發明第四種實施方式的具高溫脫附之轉輪方法，主要係設有一第一吸附轉輪410、一第二吸附轉輪420、一第一加熱裝置430、一第二加熱裝置440、一第三加熱裝置450及一第四加熱裝置460，而該第一吸附轉輪410係設有吸附區4101、冷卻區4102、脫附區4103及高溫脫附區4104，另該第二吸附轉輪420係設有吸附區4201、冷卻區4202、脫附區4203及高溫脫附區4204，因此，本發明主要在於該第一吸附轉輪410及該第二吸附轉輪420除了設有吸附區4101、4201、冷卻區4102、4202及脫附區4103、4203外，還設有高溫脫附區4104、4204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪410及該第二吸附轉輪420能恢復其吸附能力，使該第一吸附轉輪410及該第二吸附轉輪420能具有四個區域。 In addition, the rotor method with high temperature desorption according to the fourth embodiment of the present invention is mainly provided with a first adsorption runner 410, a second adsorption runner 420, a first heating device 430, and a second heating device 440 , A third heating device 450 and a fourth heating device 460, and the first adsorption runner 410 is provided with an adsorption zone 4101, a cooling zone 4102, a desorption zone 4103 and a high temperature desorption zone 4104, and the second adsorption The runner 420 is provided with an adsorption zone 4201, a cooling zone 4202, a desorption zone 4203, and a high-temperature desorption zone 4204. Therefore, the present invention mainly lies in that the first adsorption runner 410 and the second adsorption runner 420 are provided with adsorption Zones 4101, 4201, cooling zones 4102, 4202 and desorption zones 4103, 4203, there are also high-temperature desorption zones 4104, 4204, which can be used for online operation (ON LINE), the residual high-boiling organic matter ( VOC) is released, so that the first adsorption runner 410 and the second adsorption runner 420 can restore their adsorption capacity, so that the first adsorption runner 410 and the second adsorption runner 420 can have four regions.

而該第四種實施方式的主要步驟(如第10圖所示)係包括：步驟S400輸入待吸附之氣體：該第一吸附轉輪410之吸附區4101的一側A係由一廢氣進氣管路411來輸入待吸附之氣體，而該第一吸附轉輪410之吸附區4101的另一側B則透過一第一淨氣排放管路412來輸送經過吸附後之氣體；透過該第一吸附轉輪410之吸附區4101的一側A係連接一廢氣進氣管路411(如第11圖及第12圖所示)，以能由該廢氣進氣管路411來輸入待吸附之氣體，而該待吸附之氣體可以為揮發性有機化合物(VOC)、二氧化碳(CO2)、氮氣(N2)、水氣或氧氣(O2)之其中任一或複數組合之一，也可以是其他上述未表述之氣體，而該第一吸附轉輪410之吸附區4101的另一側B則與該一第一淨氣排 放管路412之一端連接(如第11圖及第12圖所示)，讓該待吸附之氣體經該第一吸附轉輪410之吸附區4101進行吸附後再由該第一淨氣排放管路412來輸送經過吸附後之氣體。而完成上述步驟S400後即進行下一步驟S410。 The main steps (as shown in FIG. 10) of the fourth embodiment include: Step S400: Input gas to be adsorbed: Side A of the adsorption zone 4101 of the first adsorption runner 410 is fed by an exhaust gas The pipeline 411 receives the gas to be adsorbed, and the other side B of the adsorption zone 4101 of the first adsorption runner 410 conveys the adsorbed gas through a first clean gas discharge pipeline 412; through the first One side A of the adsorption area 4101 of the adsorption rotor 410 is connected to an exhaust gas intake line 411 (as shown in FIGS. 11 and 12), so that the exhaust gas intake line 411 can input the gas to be adsorbed The gas to be adsorbed can be any one or a combination of volatile organic compounds (VOC), carbon dioxide (CO2), nitrogen (N2), water vapor or oxygen (O2), or other combinations of the above Expressed gas, and the other side B of the adsorption zone 4101 of the first adsorption runner 410 is discharged from the first clean gas One end of the discharge line 412 is connected (as shown in FIG. 11 and FIG. 12), so that the gas to be adsorbed is adsorbed through the adsorption area 4101 of the first adsorption runner 410 and then is discharged from the first clean gas discharge pipe Road 412 to transport the gas after adsorption. After the above step S400 is completed, the next step S410 is performed.

另，下一步進行的步驟S410輸入用來冷卻之氣體：該第一吸附轉輪410之冷卻區4102的另一側B係由一第一冷卻氣進氣管路413來輸入用來冷卻之氣體，而該第一吸附轉輪410之冷卻區4102的一側A則透過一第一冷卻氣輸送管路414來連接至該第一加熱裝置430，以將經過該第一吸附轉輪410之冷卻區4102的氣體輸送到該第一加熱裝置430內；該第一吸附轉輪410之冷卻區4102的另一側B係連接一第一冷卻氣進氣管路413(如第11圖及第12圖所示)，以供用來冷卻之氣體進入該第一吸附轉輪410之冷卻區4102來進行冷卻使用，而該第一吸附轉輪410之冷卻區4102的一側A則連接一第一冷卻氣輸送管路414(如第11圖及第12圖所示)，該第一冷卻氣輸送管路414的另一端係與該第一加熱裝置430連接，使能將經過該第一吸附轉輪410之冷卻區4102的氣體輸送到該第一加熱裝置430內。 In addition, in the next step S410, the gas used for cooling is input: the other side B of the cooling zone 4102 of the first adsorption runner 410 is supplied with a gas for cooling by a first cooling gas inlet line 413 , And the side A of the cooling zone 4102 of the first adsorption runner 410 is connected to the first heating device 430 through a first cooling gas delivery line 414 to cool the first adsorption runner 410 The gas in the zone 4102 is delivered to the first heating device 430; the other side B of the cooling zone 4102 of the first adsorption runner 410 is connected to a first cooling gas inlet line 413 (as shown in FIGS. 11 and 12 As shown in the figure), the gas used for cooling enters the cooling zone 4102 of the first adsorption runner 410 for cooling, and the side A of the cooling zone 4102 of the first adsorption runner 410 is connected to a first cooling The gas conveying pipeline 414 (as shown in FIGS. 11 and 12), the other end of the first cooling gas conveying pipeline 414 is connected to the first heating device 430, so that it can pass through the first adsorption runner The gas in the cooling zone 4102 of 410 is delivered into the first heating device 430.

而上述該第一加熱裝置430係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第一吸附轉輪410之冷卻區4102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪410之冷卻區4102的另 一側B所連接的第一冷卻氣進氣管路413乃是供新鮮空氣或外氣進入(如第11圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪410之冷卻區4102降溫用。另第二種實施態樣係該第一淨氣排放管路412係設有一第一淨氣第一連通管路484，而該第一淨氣第一連通管路484的另一端係與該第一冷卻氣進氣管路413連接(如第12圖所示)，以能透過該第一淨氣第一連通管路484來將該第一淨氣排放管路412內經過該第一吸附轉輪410之吸附區4101所吸附過後的氣體輸送到該第一吸附轉輪410之冷卻區4102以進行降溫使用，另該第一淨氣第一連通管路484係設有一第一淨氣第一連通控制閥門4841(如第12圖所示)，以控制該第一淨氣第一連通管路484的風量。而完成上述步驟S410後即進行下一步驟S420。 The above-mentioned first heating device 430 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling zone 4102 of the first adsorption runner 410 is provided with two implementations, wherein the first implementation is the cooling zone 4102 of the first adsorption runner 410. The first cooling air intake line 413 connected to side B is for fresh air or outside air to enter (as shown in FIG. 11), and the first adsorption runner 410 is provided through the fresh air or outside air The cooling zone 4102 is used for cooling. In another second embodiment, the first clean gas discharge line 412 is provided with a first clean gas first communication line 484, and the other end of the first clean gas first communication line 484 is connected to The first cooling gas intake line 413 is connected (as shown in FIG. 12) so that the first clean gas discharge line 412 can pass through the first The gas adsorbed by the adsorption zone 4101 of an adsorption runner 410 is sent to the cooling zone 4102 of the first adsorption runner 410 for cooling, and the first clean gas first communication line 484 is provided with a first The first clean air communication control valve 4841 (as shown in FIG. 12) controls the air volume of the first clean air first communication line 484. After the above step S410 is completed, the next step S420 is performed.

另，下一步進行的步驟S420輸送高溫熱氣進行脫附：該第一吸附轉輪410之脫附區4103的一側A係由一第一熱氣輸送管路415來輸送該第一加熱裝置430內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路415係設有一第一熱氣旁通管路491，透過該第一熱氣旁通管路491連接至該第二加熱裝置440，而該第一吸附轉輪410之脫附區4103的另一側B則透過一第一脫附濃縮氣體管路416來輸送經過脫附後之脫附濃縮氣體；該第一吸附轉輪410之脫附區4103的一側A係與該一第一熱氣輸送管路415連接，且該第一熱氣輸送管路415的另一端則與該第一加熱裝置430連接(如第11圖及第12圖所示)，以能將經由該第一加熱裝置430進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路415來輸送到該第一吸附轉輪410之脫 附區4103來進行脫附使用。另該第一熱氣輸送管路415係設有一第一熱氣旁通管路491，該第一熱氣旁通管路491的另一端係與該第二加熱裝置440連接(如第11圖及第12圖所示)，以能將經由該第一加熱裝置430進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路491來輸送到該第二加熱裝置440內，另該第一吸附轉輪410之脫附區4103的另一側B係連接一第一脫附濃縮氣體管路416的一端(如第11圖及第12圖所示)，以用輸送經過該第一吸附轉輪410之脫附區4103進行脫附後之脫附濃縮氣體。 In addition, in the next step S420, high-temperature hot gas is transported for desorption: side A of the desorption area 4103 of the first adsorption runner 410 is transported into the first heating device 430 by a first hot gas transport line 415 The generated high-temperature hot gas is used for desorption, and the first hot gas delivery line 415 is provided with a first hot gas bypass line 491, which is connected to the second heating device 440 through the first hot gas bypass line 491, The other side B of the desorption zone 4103 of the first adsorption runner 410 conveys the desorbed concentrated gas after desorption through a first desorption concentrated gas line 416; One side A of the desorption zone 4103 is connected to the first hot gas delivery line 415, and the other end of the first hot gas delivery line 415 is connected to the first heating device 430 (as shown in FIGS. 11 and 12 As shown in the figure), the high-temperature hot gas heated or exchanged by the first heating device 430 can be transported to the first adsorption runner 410 through the first hot gas delivery pipeline 415 Attach area 4103 for desorption use. In addition, the first hot gas delivery line 415 is provided with a first hot gas bypass line 491, and the other end of the first hot gas bypass line 491 is connected to the second heating device 440 (as shown in FIGS. 11 and 12 As shown in the figure), the high-temperature hot gas that can be heated or exchanged through the first heating device 430 can be partially shunted and sent to the second heating device 440 through the first hot gas bypass line 491, and The other side B of the desorption zone 4103 of the first adsorption runner 410 is connected to one end of a first desorption concentrated gas line 416 (as shown in FIGS. 11 and 12) for transportation through the first A desorption concentrated gas after desorption in the desorption zone 4103 of an adsorption runner 410.

而上述該第二加熱裝置440係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該第一熱氣旁通管路491係設有一第一熱氣旁通控制閥門4911(如第12圖所示)，以控制該第一熱氣旁通管路491的風量，使能將經由該第一加熱裝置430進行加熱或熱交換的高溫熱氣部分分流到該第二加熱裝置440內。而完成上述步驟S420後即進行下一步驟S430。 The above-mentioned second heating device 440 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. And the first hot gas bypass line 491 is provided with a first hot gas bypass control valve 4911 (as shown in FIG. 12) to control the air volume of the first hot gas bypass line 491 to enable the The high-temperature hot gas that is heated or exchanged by the first heating device 430 is partially shunted into the second heating device 440. After the above step S420 is completed, the next step S430 is performed.

另，下一步進行的步驟S430再將高沸點有機物脫出：該第一吸附轉輪410之高溫脫附區4104的一側A係由一第二熱氣輸送管路417來輸送由該第二加熱裝置440內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪410之高溫脫附區4104的另一側B則透過一第一高溫脫附濃縮氣體管路418來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路416內；該第 一吸附轉輪410之高溫脫附區4104的一側A係與一第二熱氣輸送管路417的一端連接，且該第二熱氣輸送管路417的另一端係與該第二加熱裝置440連接(如第11圖及第12圖所示)，透過該第二加熱裝置440來將進入該第二熱氣輸送管路417內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路417內的高溫熱氣再輸送到該第一吸附轉輪410之高溫脫附區4104，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪410能恢復其吸附能力，另該第一吸附轉輪410之高溫脫附區4104的另一側B係連接一第一高溫脫附濃縮氣體管路418(如第11圖及第12圖所示)，而該第一高溫脫附濃縮氣體管路418的另一端係與該第一脫附濃縮氣體管路416連接，以將經過該第一吸附轉輪410之高溫脫附區4104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路418來輸送到該第一脫附濃縮氣體管路416內。 In addition, the next step S430 is to remove the high-boiling organic matter: the side A of the high-temperature desorption zone 4104 of the first adsorption runner 410 is conveyed by a second hot gas conveying line 417 by the second heating The high temperature hot gas raised to a certain temperature in the device 440 to remove high boiling point organic compounds (VOC), and the other side B of the high temperature desorption zone 4104 of the first adsorption runner 410 is desorbed through a first high temperature The concentrated gas pipeline 418 is used to transport the high-temperature desorbed concentrated gas after desorption to the first desorbed concentrated gas pipeline 416; the first One side A of the high-temperature desorption zone 4104 of an adsorption runner 410 is connected to one end of a second hot gas delivery pipe 417, and the other end of the second hot gas delivery pipe 417 is connected to the second heating device 440 (As shown in Figure 11 and Figure 12), through the second heating device 440, the high-temperature hot gas entering the second hot gas delivery pipe 417 can be raised to a certain temperature (for example, 300°C), and the second The hot gas in the hot gas delivery pipeline 417 is sent to the high temperature desorption area 4104 of the first adsorption runner 410 for high temperature desorption. When it is online (ON LINE), the remaining high boiling point can be removed Organic matter (VOC) is desorbed, so that the first adsorption runner 410 can restore its adsorption capacity, and the other side of the high temperature desorption zone 4104 of the first adsorption runner 410 is connected to a first high temperature desorption concentrated gas Pipeline 418 (as shown in FIGS. 11 and 12), and the other end of the first high-temperature desorption concentrated gas pipeline 418 is connected to the first desorption concentrated gas pipeline 416 to pass the The high-temperature desorption concentrated gas desorbed by the high-temperature desorption zone 4104 of an adsorption runner 410 can be transported into the first desorption concentrated gas line 416 through the first high-temperature desorption concentrated gas line 418.

而上述該第一脫附濃縮氣體管路416的另一端係與一焚燒裝置400連接(如第11圖及第12圖所示)，其中該焚燒裝置400係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第四種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置400乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置400不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置400為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口401及出口402，而該入 口401係與該第一脫附濃縮氣體管路416連接，其中該第一脫附濃縮氣體管路416另有與該第一高溫脫附濃縮氣體管路418的另一端連接，以將經過該第一吸附轉輪410之高溫脫附區4104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路418來輸送到該第一脫附濃縮氣體管路416內，使該第一脫附濃縮氣體管路416內除了經過該第一吸附轉輪410之脫附區4103所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路416內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口402則連接至一煙囪470(如第11圖及第12圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪470來排出，另該第一脫附濃縮氣體管路416係設有一風機4161(如第12圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口401內，讓脫附濃縮氣體能進行高溫裂解。而完成上述步驟S430後即進行下一步驟S440。 The other end of the first desorption concentrated gas pipeline 416 is connected to an incinerator 400 (as shown in FIGS. 11 and 12), wherein the incinerator 400 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown), or regenerative incinerator (RTO), and the illustration of the fourth embodiment of the present invention takes the regenerative incinerator (RTO) as an example, The incinerator 400 described below is a regenerative incinerator (RTO), but the incinerator 400 of the present invention is not limited to a regenerative incinerator (RTO), but may also be a direct combustion incinerator (TO) (FIG. Not shown) or catalyst furnace (not shown). When the incinerator 400 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 401 and an outlet 402, and the inlet The port 401 is connected to the first desorption concentrated gas line 416, wherein the first desorption concentrated gas line 416 is further connected to the other end of the first high-temperature desorption concentrated gas line 418 to pass through the The high-temperature desorption concentrated gas desorbed by the high-temperature desorption zone 4104 of the first adsorption runner 410 can be transported into the first desorption concentrated gas line 416 through the first high-temperature desorption concentrated gas line 418, The first desorption concentrated gas pipeline 416 contains high-temperature desorption concentrated gas in addition to the desorption concentrated gas desorbed through the desorption zone 4103 of the first adsorption runner 410, so that the high-temperature desorption concentrated gas It can enter the regenerative incinerator (RTO) together with the desorbed concentrated gas in the first desorbed concentrated gas line 416 for high-temperature cracking to reduce volatile organic compounds, and the regenerative incinerator (RTO) The outlet 402 is connected to a chimney 470 (as shown in Figure 11 and Figure 12), so that the clean gas after the high temperature cracking of organic compounds can be discharged from the chimney 470, and the first desorption concentrated gas pipe The road 416 is equipped with a fan 4161 (as shown in Figure 12) to push and pull the desorbed concentrated gas into the inlet 401 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to undergo high-temperature cracking. After the above step S430 is completed, the next step S440 is performed.

另，下一步進行的步驟S440輸送欲再吸附之氣體：該第二吸附轉輪420之吸附區4201的一側A係由該第一淨氣排放管路412來輸送欲進行再吸附之氣體，而該第二吸附轉輪420之吸附區4201的另一側B則透過一第二淨氣排放管路421來輸送經過再吸附後之氣體；該第二吸附轉輪420之吸附區4201的一側A係與該第一淨氣排放管路412的另一端相連接(如第11圖及第12圖所示)，使該第一淨氣排放管路412內經過吸附後之氣體能直接再輸送到該第二吸附轉輪 420之吸附區4201內進行再吸附，另該第二吸附轉輪420之吸附區4201的另一側B係連接一第二淨氣排放管路421，並透過該第二淨氣排放管路421來輸送經過再吸附後之氣體。 In addition, the next step S440 conveys the gas to be re-adsorbed: the side A of the adsorption area 4201 of the second adsorption runner 420 is conveyed by the first clean gas discharge line 412 to the gas to be re-adsorbed, The other side B of the adsorption zone 4201 of the second adsorption runner 420 conveys the re-adsorbed gas through a second clean gas discharge line 421; one of the adsorption zones 4201 of the second adsorption runner 420 Side A is connected to the other end of the first clean gas discharge line 412 (as shown in FIG. 11 and FIG. 12), so that the adsorbed gas in the first clean gas discharge line 412 can be directly recycled Conveyed to the second adsorption runner Re-adsorption is performed in the adsorption zone 4201 of 420, and the other side B of the adsorption zone 4201 of the second adsorption runner 420 is connected to a second clean gas discharge line 421 and passes through the second clean gas discharge line 421 To transport the gas after re-adsorption.

而上述該第二淨氣排放管路421之另一端則與一煙囪470連接(如第11圖及第12圖所示)，以方便將經由該第一吸附轉輪410之吸附區4101及該第二吸附轉輪420之吸附區4201所吸附過後之氣體透過該煙囪470來進行排放，其中該第二淨氣排放管路421係設有一風機4211(如第12圖所示)，以增加氣體之流速來流向該煙囪470。而完成上述步驟S440後即進行下一步驟S450。 The other end of the second clean gas discharge line 421 is connected to a chimney 470 (as shown in FIGS. 11 and 12 ), so as to facilitate the adsorption area 4101 passing through the first adsorption runner 410 and the The gas adsorbed by the adsorption area 4201 of the second adsorption runner 420 is discharged through the chimney 470, wherein the second clean gas discharge line 421 is provided with a fan 4211 (as shown in FIG. 12) to increase the gas The flow velocity comes to the chimney 470. After the above step S440 is completed, the next step S450 is performed.

另，下一步進行的步驟S450輸入用來冷卻之氣體：該第二吸附轉輪420之冷卻區4202的一側A係由一第二冷卻氣進氣管路422來輸入用來冷卻之氣體，而該第二吸附轉輪420之冷卻區4202的另一側B則透過一第二冷卻氣輸送管路423來連接至該第三加熱裝置450，以將經過該第二吸附轉輪420之冷卻區4202的氣體輸送到該第三加熱裝置450內；該第二吸附轉輪420之冷卻區4202的一側A係連接一第二冷卻氣進氣管路422(如第11圖及第12圖所示)，以供用來冷卻之氣體進入該第二吸附轉輪420之冷卻區4202來進行冷卻使用，而該第二吸附轉輪420之冷卻區4202的另一側B則連接一第二冷卻氣輸送管路423(如第11圖及第12圖所示)，該第二冷卻氣輸送管路423的另一端係與該第三加熱裝置450連接，使能將經過該第二吸附轉輪420之冷卻區4202的氣體輸送到該第三加熱裝置450內。 In addition, in the next step S450, the gas used for cooling is input: the side A of the cooling area 4202 of the second adsorption runner 420 is supplied with a gas for cooling by a second cooling gas inlet line 422, The other side B of the cooling zone 4202 of the second adsorption runner 420 is connected to the third heating device 450 through a second cooling gas delivery line 423 to cool the passing of the second adsorption runner 420 The gas in zone 4202 is delivered to the third heating device 450; the side A of the cooling zone 4202 of the second adsorption runner 420 is connected to a second cooling gas inlet line 422 (as shown in FIGS. 11 and 12) (Shown), for the gas used for cooling to enter the cooling zone 4202 of the second adsorption runner 420 for cooling, and the other side B of the cooling zone 4202 of the second adsorption runner 420 is connected to a second cooling The gas conveying pipeline 423 (as shown in FIGS. 11 and 12), the other end of the second cooling gas conveying pipeline 423 is connected to the third heating device 450, enabling the passing of the second adsorption runner The gas in the cooling zone 4202 of 420 is delivered into the third heating device 450.

而上述該第三加熱裝置450係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該第二吸附轉輪420之冷卻區4202係設有兩種實施態樣，其中第一種實施態樣為該第二吸附轉輪之420冷卻區4202的一側A所連接的第二冷卻氣進氣管路422乃是供新鮮空氣或外氣進入(如第11圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪420之冷卻區4202降溫用。另第二種實施態樣係該第一淨氣排放管路412係設有一第一淨氣第二連通管路485，而該第一淨氣第二連通管路485的另一端係與該第二冷卻氣進氣管路422連接(如第12圖所示)，以能透過該第一淨氣第二連通管路485來將該第一淨氣排放管路412內的氣體輸送到該第二吸附轉輪420之冷卻區4202以進行降溫使用，另該第一淨氣第二連通管路485係設有一第一淨氣第二連通控制閥門4851，以控制該第一淨氣第二連通管路485的風量。而完成上述步驟S450後即進行下一步驟S460。 The above-mentioned third heating device 450 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling zone 4202 of the second adsorption runner 420 is provided with two implementation forms, wherein the first implementation form is the second connected to the side A of the cooling zone 4202 of the second adsorption runner 420 The cooling gas inlet line 422 is for fresh air or outside air to enter (as shown in FIG. 11), and provides cooling temperature 4202 of the second adsorption runner 420 through the fresh air or outside air for cooling. In another second embodiment, the first clean gas discharge line 412 is provided with a first clean gas second communication line 485, and the other end of the first clean gas second communication line 485 is connected to the first The second cooling gas inlet line 422 is connected (as shown in FIG. 12) so that the gas in the first clean gas discharge line 412 can be sent to the first through the first clean gas second communication line 485 The cooling zone 4202 of the two adsorption runners 420 is used for cooling. In addition, the first clean gas second communication line 485 is provided with a first clean gas second communication control valve 4851 to control the first clean gas second communication The air volume of the pipeline 485. After the above step S450 is completed, the next step S460 is performed.

另，下一步進行的步驟S460輸送高溫熱氣進行脫附：該第二吸附轉輪420之脫附區4203的另一側B係由一第三熱氣輸送管路424來輸送該第三加熱裝置450內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路424係設有一第三熱氣旁通管路492，透過該第三熱氣旁通管路492連接至該第四加熱裝置460，而該第二吸附轉輪420之脫附區4203的一側A則透過一第二脫附濃縮氣體管路425來輸送經過脫附後之脫附濃縮氣體；該第二吸附轉輪420之脫附區4 203的另一側B係與該一第三熱氣輸送管路424連接，且該第三熱氣輸送管路424的另一端則與該第三加熱裝置450連接(如第11圖及第12圖所示)，以能將經由該第三加熱裝置450進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路424來輸送到該第二吸附轉輪420之脫附區4203來進行脫附使用。另該第三熱氣輸送管路424係設有一第三熱氣旁通管路492(如第11圖及第12圖所示)，該第三熱氣旁通管路492的另一端係與該第四加熱裝置460連接，以能將經由該第三加熱裝置450進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路492來輸送到該第四加熱裝置460內，另該第二吸附轉輪420之脫附區4203的一側A係連接一第二脫附濃縮氣體管路425的一端(如第11圖及第12圖所示)，以用輸送經過該第二吸附轉輪420之脫附區4203進行脫附後之脫附濃縮氣體。 In addition, the next step S460 is to transport high-temperature hot gas for desorption: the other side B of the desorption zone 4203 of the second adsorption runner 420 is transported by a third hot gas delivery pipeline 424 to the third heating device 450 The high-temperature hot gas generated therein is used for desorption, and the third hot gas delivery pipeline 424 is provided with a third hot gas bypass pipeline 492, which is connected to the fourth heating device 460 through the third hot gas bypass pipeline 492 , And the side A of the desorption zone 4203 of the second adsorption runner 420 conveys the desorbed concentrated gas after desorption through a second desorption concentrated gas line 425; the second adsorption runner 420 Desorption Zone 4 The other side B of 203 is connected to the third hot gas delivery line 424, and the other end of the third hot gas delivery line 424 is connected to the third heating device 450 (as shown in FIGS. 11 and 12) (Show)), the high-temperature hot gas heated or exchanged by the third heating device 450 can be transported to the desorption area 4203 of the second adsorption runner 420 through the third hot gas delivery pipeline 424 for desorption . In addition, the third hot gas delivery line 424 is provided with a third hot gas bypass line 492 (as shown in FIGS. 11 and 12), and the other end of the third hot gas bypass line 492 is connected to the fourth The heating device 460 is connected so that the high-temperature hot gas that is heated or exchanged through the third heating device 450 can be partially shunted, and is transferred into the fourth heating device 460 through the third hot gas bypass line 492, and One side A of the desorption zone 4203 of the second adsorption runner 420 is connected to one end of a second desorption concentrated gas line 425 (as shown in FIG. 11 and FIG. 12) for transportation through the second The desorption concentrated gas after the desorption zone 4203 of the adsorption rotor 420 is desorbed.

而上述該第四加熱裝置460係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該第三熱氣旁通管路492係設有一第三熱氣旁通控制閥門4921(如第12圖所示)，以控制該第三熱氣旁通管路492的風量，使能將經由該第三加熱裝置450進行加熱或熱交換的高溫熱氣部分分流到該第四加熱裝置460內。而完成上述步驟S460後即進行下一步驟S470。 The above-mentioned fourth heating device 460 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. And the third hot gas bypass line 492 is provided with a third hot gas bypass control valve 4921 (as shown in FIG. 12) to control the air volume of the third hot gas bypass line 492, so that The high-temperature hot gas that is heated or exchanged by the third heating device 450 is partially shunted into the fourth heating device 460. After the above step S460 is completed, the next step S470 is performed.

另，下一步進行的步驟S470再將高沸點有機物脫出：該第二吸附轉輪420之高溫脫附區4204的另一側B係由一第四熱氣輸 送管路426來輸送由該第四加熱裝置460內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪420之高溫脫附區4204的一側A則透過一第二高溫脫附濃縮氣體管路427來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路425內；該第二吸附轉輪420之高溫脫附區4204的另一側B係與一第四熱氣輸送管路426的一端連接，且該第四熱氣輸送管路426的另一端係與該第四加熱裝置460連接(如第11圖及第12圖所示)，透過該第四加熱裝置460來將進入該第四熱氣輸送管路426內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路426內的高溫熱氣再輸送到該第二吸附轉輪420之高溫脫附區4204，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪420能恢復其吸附能力，另該第二吸附轉輪420之高溫脫附區4204的一側A係連接一第二高溫脫附濃縮氣體管路427(如第11圖及第12圖所示)，而該第二高溫脫附濃縮氣體管路427的另一端係與該第二脫附濃縮氣體管路425連接，以將經過該第二吸附轉輪420之高溫脫附區4204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路427來輸送到該第二脫附濃縮氣體管路425內。 In addition, in the next step S470, the high-boiling organic matter is removed again: the other side B of the high-temperature desorption zone 4204 of the second adsorption runner 420 is transported by a fourth hot gas A pipeline 426 is used to transport high-temperature hot gas raised to a certain temperature by the fourth heating device 460 to remove high-boiling organic compounds (VOC), and a high-temperature desorption zone 4204 of the second adsorption runner 420 Side A conveys the high-temperature desorption concentrated gas after desorption through a second high-temperature desorption concentrated gas line 427 to the second desorption concentrated gas line 425; the high-temperature desorption of the second adsorption runner 420 The other side B of the attached zone 4204 is connected to one end of a fourth hot gas delivery line 426, and the other end of the fourth hot gas delivery line 426 is connected to the fourth heating device 460 (as shown in FIGS. 11 and 12)), through the fourth heating device 460, the high temperature hot gas entering the fourth hot gas delivery pipeline 426 can be raised to a certain temperature (for example, 300 ℃), and the fourth hot gas delivery pipeline 426 The high-temperature hot gas is transported to the high-temperature desorption zone 4204 of the second adsorption runner 420 for high-temperature desorption. When online operation (ON LINE), the remaining high-boiling organic matter (VOC) can be removed. The second adsorption runner 420 can restore its adsorption capacity, and the side A of the high temperature desorption zone 4204 of the second adsorption runner 420 is connected to a second high temperature desorption concentrated gas line 427 (as shown in FIG. 11 And FIG. 12), and the other end of the second high temperature desorption concentrated gas line 427 is connected to the second desorption concentrated gas line 425 to remove the high temperature passing through the second adsorption runner 420 The high-temperature desorption concentrated gas desorbed in the attachment zone 4204 can be transported into the second desorption concentrated gas line 425 through the second high-temperature desorption concentrated gas line 427.

而上述該第二脫附濃縮氣體管路425的另一端係與一焚燒裝置400連接(如第11圖及第12圖所示)，其中該焚燒裝置400係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第四種實施方式之圖示係以蓄熱式焚燒爐(RTO)為 例，且下面說明的焚燒裝置400乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置400不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置400為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口401及出口402，而該入口401係與該第二脫附濃縮氣體管路425連接，其中該第二脫附濃縮氣體管路425另有與該第二高溫脫附濃縮氣體管路427的另一端連接，以將經過該第二吸附轉輪420之高溫脫附區4204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路427來輸送到該第二脫附濃縮氣體管路425內，使該第二脫附濃縮氣體管路425內除了經過該第二吸附轉輪420之脫附區4203所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路425內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口402則連接至一煙囪470(如第11圖及第12圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪470來排出，另該第二脫附濃縮氣體管路425係設有一風機4251(如第12圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口401內，讓脫附濃縮氣體能進行高溫裂解。 The other end of the second desorption concentrated gas pipeline 425 is connected to an incinerator 400 (as shown in FIGS. 11 and 12), wherein the incinerator 400 is a direct combustion incinerator (TO) (Not shown), catalyst furnace (not shown) or regenerative incinerator (RTO), and the illustration of the fourth embodiment of the present invention is based on regenerative incinerator (RTO) as For example, and the incinerator 400 described below is a regenerative incinerator (RTO), but the incinerator 400 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (Not shown) or catalyst furnace (not shown). When the incinerator 400 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 401 and an outlet 402, and the inlet 401 is connected to the second desorption concentrated gas pipeline 425 , Wherein the second desorption concentrated gas pipeline 425 is additionally connected to the other end of the second high-temperature desorption concentrated gas pipeline 427 to desorb the high-temperature desorption zone 4204 passing through the second adsorption runner 420 The lower high-temperature desorption concentrated gas can be transported into the second desorption concentrated gas line 425 through the second high-temperature desorption concentrated gas line 427, so that the second desorption concentrated gas line 425 passes through the The desorption concentrated gas desorbed by the desorption zone 4203 of the second adsorption runner 420 also contains high-temperature desorption concentrated gas, so that the high-temperature desorption concentrated gas can be desorbed from the second desorption concentrated gas pipeline 425 The concentrated gas enters the regenerative incinerator (RTO) for high temperature cracking to reduce volatile organic compounds, and the outlet 402 of the regenerative incinerator (RTO) is connected to a chimney 470 (as shown in Figure 11 and (Shown in Figure 12), so that the clean gas after pyrolysis of organic compounds can be discharged from the chimney 470, and the second desorption concentrated gas pipeline 425 is provided with a fan 4251 (as shown in Figure 12) In order to push the desorbed concentrated gas into the inlet 401 of the regenerative incinerator (RTO), the desorbed concentrated gas can be cracked at high temperature.

另本發明第四種實施架構的具高溫脫附之轉輪系統(如第11圖及第12圖所示)，主要係透過一第一吸附轉輪410、一第二吸附轉輪420、一第一加熱裝置430、一第二加熱裝置440、一第三加熱裝置450及一第四加熱裝置460之組合設計，而本發明第四種實施架 構的第一吸附轉輪410係設有吸附區4101、冷卻區4102、脫附區4103及高溫脫附區4104，該第一吸附轉輪410係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且一廢氣進氣管路411係連接至該第一吸附轉輪410之吸附區4101的一側A(如第11圖及第12圖所示)，以使該第一吸附轉輪410之吸附區4101能吸附該廢氣進氣管路411內的有機物，而該第一吸附轉輪410之吸附區4101的另一側B係與該一第一淨氣排放管路412之一端連接，讓該廢氣經該第一吸附轉輪410之吸附區4101進行吸附有機物後再由該第一淨氣排放管路412來輸送。 In addition, the fourth implementation framework of the present invention for a high-temperature desorption rotor system (as shown in FIGS. 11 and 12) is mainly through a first adsorption runner 410, a second adsorption runner 420, a The combined design of the first heating device 430, a second heating device 440, a third heating device 450 and a fourth heating device 460, and the fourth embodiment of the present invention The structured first adsorption runner 410 is provided with an adsorption zone 4101, a cooling zone 4102, a desorption zone 4103, and a high-temperature desorption zone 4104. The first adsorption runner 410 is a zeolite concentration runner or other material concentration rotor And an exhaust gas intake line 411 is connected to the side A (as shown in FIGS. 11 and 12) of the adsorption zone 4101 of the first adsorption runner 410, so that the first adsorption runner 410 The adsorption zone 4101 can adsorb organic matter in the exhaust gas inlet line 411, and the other side B of the adsorption zone 4101 of the first adsorption runner 410 is connected to one end of the first clean gas discharge line 412, The exhaust gas is allowed to pass through the adsorption zone 4101 of the first adsorption runner 410 to adsorb organic matter, and then is transported by the first clean gas discharge line 412.

另該第一吸附轉輪410之冷卻區4102的另一側B係連接一第一冷卻氣進氣管路413(如第11圖及第12圖所示)，以供氣體進入該第一吸附轉輪410之冷卻區4102來進行冷卻使用，而該第一吸附轉輪410之冷卻區4102的一側A係連接一第一冷卻氣輸送管路414(如第11圖及第12圖所示)，該第一冷卻氣輸送管路414的另一端係與該第一加熱裝置430連接，其中該第一加熱裝置430係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第一熱氣輸送管路415的一端係與該第一吸附轉輪410之脫附區4103的一側A連接(如第11圖及第12圖所示)，且該第一熱氣輸送管路415的另一端則與該第一加熱裝置430連接，以能將經由該第一加熱裝置430進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路415來輸送到該第一吸附轉輪410之 脫附區4103來進行脫附使用。 In addition, the other side B of the cooling zone 4102 of the first adsorption runner 410 is connected to a first cooling gas intake line 413 (as shown in FIGS. 11 and 12) for the gas to enter the first adsorption The cooling zone 4102 of the runner 410 is used for cooling, and one side A of the cooling zone 4102 of the first adsorption runner 410 is connected to a first cooling gas delivery line 414 (as shown in FIGS. 11 and 12) ), the other end of the first cooling gas delivery line 414 is connected to the first heating device 430, wherein the first heating device 430 is any one of a heater, a pipe heater or a heat exchanger, the heating The heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the duct heater (not shown) is any one of using gas fuel or liquid fuel. One end of the first hot gas delivery line 415 is connected to the side A of the desorption zone 4103 of the first adsorption runner 410 (as shown in FIGS. 11 and 12), and the first hot gas delivery The other end of the pipeline 415 is connected to the first heating device 430, so that the high-temperature hot gas heated or exchanged through the first heating device 430 can be transported to the first adsorption through the first hot gas transport line 415 Runner 410 The desorption area 4103 is used for desorption.

而上述該第一吸附轉輪410之冷卻區4102係設有兩種實施態樣，其中第一種實施態樣為該第一吸附轉輪410之冷卻區4102的另一側B所連接的第一冷卻氣進氣管路413乃是供新鮮空氣或外氣進入(如第11圖所示)，透過該新鮮空氣或外氣來提供該第一吸附轉輪410之冷卻區4102降溫用。另第二種實施態樣係該第一淨氣排放管路412係設有一第一淨氣第一連通管路484，而該第一淨氣第一連通管路484的另一端係與該第一冷卻氣進氣管路413連接(如第12圖所示)，以能透過該第一淨氣第一連通管路484來將該第一淨氣排放管路412內經過該第一吸附轉輪410之吸附區4101所吸附過後的氣體輸送到該第一吸附轉輪410之冷卻區4102以進行降溫使用，另該第一淨氣第一連通管路484係設有一第一淨氣第一連通控制閥門4841(如第12圖所示)，以控制該第一淨氣第一連通管路484的風量。 The cooling zone 4102 of the first adsorption runner 410 is provided with two implementations, of which the first implementation is the connection of the other side B of the cooling zone 4102 of the first adsorption runner 410. A cooling air intake line 413 is for fresh air or outside air to enter (as shown in FIG. 11), and provides cooling temperature 4102 of the first adsorption runner 410 through the fresh air or outside air for cooling. In another second embodiment, the first clean gas discharge line 412 is provided with a first clean gas first communication line 484, and the other end of the first clean gas first communication line 484 is connected to The first cooling gas intake line 413 is connected (as shown in FIG. 12) so that the first clean gas discharge line 412 can pass through the first The gas adsorbed by the adsorption zone 4101 of an adsorption runner 410 is sent to the cooling zone 4102 of the first adsorption runner 410 for cooling, and the first clean gas first communication line 484 is provided with a first The first clean air communication control valve 4841 (as shown in FIG. 12) controls the air volume of the first clean air first communication line 484.

另該一第一脫附濃縮氣體管路416的一端係與該第一吸附轉輪410之脫附區4103的另一側B連接，而該第一脫附濃縮氣體管路416的另一端係與一焚燒裝置400連接(如第11圖及第12圖所示)，其中該焚燒裝置400係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第四種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置400乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置400不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置400為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口40 1及出口402，而該入口401係與該第一脫附濃縮氣體管路416連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第一脫附濃縮氣體管路416來輸送到該蓄熱式焚燒爐(RTO)之入口401，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口402則連接至一煙囪470(如第11圖及第12圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪470來排出，另該第一脫附濃縮氣體管路416係設有一風機4161，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口401內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the first desorption concentrated gas line 416 is connected to the other side B of the desorption zone 4103 of the first adsorption runner 410, and the other end of the first desorption concentrated gas line 416 is Connected to an incinerator 400 (as shown in Figure 11 and Figure 12), where the incinerator 400 is a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or heat storage Of any type of incinerator (RTO), and the illustration of the fourth implementation structure of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 400 described below is a regenerative incinerator (RTO) ), but the incinerator 400 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 400 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 40 1 and outlet 402, and the inlet 401 is connected to the first desorption concentrated gas pipeline 416, so that the desorbed concentrated gas desorbed by high temperature can be transported through the first desorption concentrated gas pipeline 416 Go to the inlet 401 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to enter the regenerative incinerator (RTO) for high-temperature cracking to reduce volatile organic compounds. In addition, the regenerative incinerator (RTO) The outlet 402 is connected to a chimney 470 (as shown in Figures 11 and 12), so that the clean gas after high-temperature cracking of organic matter can be discharged from the chimney 470, and the first desorption concentrated gas pipeline 416 is equipped with a fan 4161, which can push and pull the desorbed concentrated gas into the inlet 401 of the regenerative incinerator (RTO), so that the desorbed concentrated gas can be pyrolyzed at high temperature.

而本發明第四種實施架構(如第11圖及第12圖所示)中主要在於該第一吸附轉輪410除了設有吸附區4101、冷卻區4102及脫附區4103外，還設有高溫脫附區4104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第一吸附轉輪410能恢復其吸附能力，使該第一吸附轉輪410能具有四個區域。而該第一吸附轉輪410之高溫脫附區4104的一側A係與一第二熱氣輸送管路417的一端連接，且該第二熱氣輸送管路417的另一端係與該第二加熱裝置440連接(如第11圖及第12圖所示)，其中該第二加熱裝置440係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第一熱氣輸送管路415係設有一第一熱氣旁通管路491，該第一熱氣旁通管路491的另一端係與該第二加熱裝置440連接(如第11圖及第12圖所示)， 以能將經由該第一加熱裝置430進行加熱或熱交換的高溫熱氣能部分分流，並透過該第一熱氣旁通管路491來輸送到該第二加熱裝置440內，以將進入該第二熱氣輸送管路417內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路417內的高溫熱氣再輸送到該第一吸附轉輪410之高溫脫附區4104，以供進行高溫脫附使用，另該第一熱氣旁通管路491係設有一第一熱氣旁通控制閥門4911(如第12圖所示)，以控制該第一熱氣旁通管路491的風量。 The fourth implementation structure of the present invention (as shown in FIG. 11 and FIG. 12) mainly lies in that the first adsorption runner 410 is provided with an adsorption zone 4101, a cooling zone 4102 and a desorption zone 4103. The high-temperature desorption zone 4104 can be used to remove the remaining high-boiling organic compounds (VOC) during ON LINE operation, so that the first adsorption runner 410 can restore its adsorption capacity, so that the first adsorption The runner 410 can have four areas. One side A of the high-temperature desorption zone 4104 of the first adsorption runner 410 is connected to one end of a second hot gas delivery line 417, and the other end of the second hot gas delivery line 417 is connected to the second heating The device 440 is connected (as shown in FIGS. 11 and 12), wherein the second heating device 440 is any one of a heater, a pipe heater, or a heat exchanger, and the heater (not shown) is Any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown in the figure) is any one using gas fuel or liquid fuel. The first hot gas delivery line 415 is provided with a first hot gas bypass line 491, and the other end of the first hot gas bypass line 491 is connected to the second heating device 440 (as shown in FIGS. 11 and 12 (Pictured), The high-temperature hot gas that can be heated or exchanged through the first heating device 430 can be partially diverted and transported into the second heating device 440 through the first hot gas bypass line 491 to enter the second The high-temperature hot gas in the hot-gas transport line 417 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the second hot-gas transport line 417 is sent to the high-temperature desorption area 4104 of the first adsorption runner 410, For use in high temperature desorption, the first hot gas bypass line 491 is provided with a first hot gas bypass control valve 4911 (as shown in FIG. 12) to control the first hot gas bypass line 491 Air volume.

再者，該第一吸附轉輪410之高溫脫附區4104的另一側B係連接一第一高溫脫附濃縮氣體管路418(如第11圖及第12圖所示)，而該第一高溫脫附濃縮氣體管路418的另一端係與該第一脫附濃縮氣體管路416連接，以將經過該第一吸附轉輪410之高溫脫附區4104所脫附下來的高溫脫附濃縮氣體能透過該第一高溫脫附濃縮氣體管路418來輸送到該第一脫附濃縮氣體管路416內，再透過該第一脫附濃縮氣體管路416輸送到該蓄熱式焚燒爐(RTO)之入口401，讓高溫脫附濃縮氣體能與該第一脫附濃縮氣體管路416內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, the other side B of the high temperature desorption zone 4104 of the first adsorption runner 410 is connected to a first high temperature desorption concentrated gas pipeline 418 (as shown in FIGS. 11 and 12), and the first The other end of a high temperature desorption concentrated gas pipeline 418 is connected to the first desorption concentrated gas pipeline 416 to desorb the high temperature desorbed by the high temperature desorption zone 4104 of the first adsorption runner 410 The concentrated gas can be transported into the first desorption concentrated gas line 416 through the first high-temperature desorption concentrated gas line 418, and then transferred to the regenerative incinerator through the first desorption concentrated gas line 416 ( The inlet 401 of the RTO) allows the high-temperature desorbed concentrated gas to enter the regenerative incinerator (RTO) together with the desorbed concentrated gas in the first desorbed concentrated gas line 416 for high-temperature cracking.

另該第二吸附轉輪420係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且該第二吸附轉輪420內係設有吸附區4201、冷卻區4202、脫附區4203及高溫脫附區4204，而該第二吸附轉輪420之吸附區4201的一側A係與該第一淨氣排放管路412的另一端相連接(如第11圖及第12圖所示)，使該第一淨氣排放管路412內的氣體能直接再輸送到該第二吸附轉輪420之吸附區4201內進行吸 附，另該第二吸附轉輪420之吸附區4201的另一側B係連接一第二淨氣排放管路421，而該第二淨氣排放管路421之另一端則與一煙囪470連接(如第11圖及第12圖所示)，以方便將經由該第一吸附轉輪410之吸附區4101及該第二吸附轉輪420之吸附區4201所吸附過的氣體透過該煙囪470來進行排放，其中該第二淨氣排放管路421係設有一風機4211(如第12圖所示)，以增加氣體之流速來流向該煙囪470。 In addition, the second adsorption runner 420 is a zeolite concentration runner or a concentration runner of other materials, and the second adsorption runner 420 is provided with an adsorption zone 4201, a cooling zone 4202, a desorption zone 4203, and a high temperature desorption Attached area 4204, and one side A of the adsorption area 4201 of the second adsorption runner 420 is connected to the other end of the first clean gas discharge line 412 (as shown in FIGS. 11 and 12), so that The gas in the first clean gas discharge line 412 can be directly sent to the adsorption area 4201 of the second adsorption rotor 420 for suction Attached, another side B of the adsorption zone 4201 of the second adsorption runner 420 is connected to a second clean gas discharge line 421, and the other end of the second clean gas discharge line 421 is connected to a chimney 470 (As shown in Figure 11 and Figure 12), to facilitate the gas adsorbed by the adsorption zone 4101 of the first adsorption runner 410 and the adsorption zone 4201 of the second adsorption runner 420 through the chimney 470 For the discharge, the second clean gas discharge line 421 is provided with a fan 4211 (as shown in FIG. 12) to increase the flow velocity of the gas to the chimney 470.

另該第二吸附轉輪420之冷卻區4202的一側A係連接一第二冷卻氣進氣管路422，以供氣體進入該第二吸附轉輪420之冷卻區4202來進行冷卻使用，而該第二吸附轉輪420之冷卻區4202的另一側B係連接一第二冷卻氣輸送管路423(如第11圖及第12圖所示)，該第二冷卻氣輸送管路423的另一端係與該第三加熱裝置450連接，其中該第三加熱裝置450係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第三熱氣輸送管路424的一端係與該第二吸附轉輪420之脫附區4203的另一側B連接，且該第三熱氣輸送管路424的另一端係與該第三加熱裝置450連接(如第11圖及第12圖所示)，以能將經由該第三加熱裝置450進行加熱或熱交換的高溫熱氣透過該第三熱氣輸送管路424來輸送到該第二吸附轉輪420之脫附區4203來進行脫附使用。 In addition, one side A of the cooling zone 4202 of the second adsorption runner 420 is connected to a second cooling gas inlet line 422 for gas to enter the cooling zone 4202 of the second adsorption runner 420 for cooling, and The other side B of the cooling zone 4202 of the second adsorption runner 420 is connected to a second cooling gas delivery line 423 (as shown in FIGS. 11 and 12). The other end is connected to the third heating device 450, wherein the third heating device 450 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is an electric heating wire or an electric heater Either a tube or an electric heating plate, the pipe heater (not shown) is either gas fuel or liquid fuel. One end of the third hot gas delivery line 424 is connected to the other side B of the desorption zone 4203 of the second adsorption runner 420, and the other end of the third hot gas delivery line 424 is connected to the third The heating device 450 is connected (as shown in FIGS. 11 and 12) so that high-temperature hot gas heated or heat-exchanged by the third heating device 450 can be transported to the second through the third hot gas delivery line 424 The desorption area 4203 of the adsorption rotor 420 is used for desorption.

而上述該第二吸附轉輪420之冷卻區4202係設有兩 種實施態樣，其中第一種實施態樣為該第二吸附轉輪420之冷卻區4202的一側A所連接的第二冷卻氣進氣管路422乃是供新鮮空氣或外氣進入(如第11圖所示)，透過該新鮮空氣或外氣來提供該第二吸附轉輪120之冷卻區4202降溫用。另第二種實施態樣係該第一淨氣排放管路412係設有一第一淨氣第二連通管路485，而該第一淨氣第二連通管路485的另一端係與該第二冷卻氣進氣管路422連接(如第12圖所示)，以能透過該第一淨氣第二連通管路485來將該第一淨氣排放管路412內的氣體輸送到該第二吸附轉輪420之冷卻區4202以進行降溫使用，另該第一淨氣第二連通管路485係設有一第一淨氣第二連通控制閥門4851(如第12圖所示)，以控制該第一淨氣第二連通管路485的風量。 The cooling area 4202 of the second adsorption runner 420 is provided with two An implementation aspect, wherein the first implementation aspect is that the second cooling air intake line 422 connected to the side A of the cooling area 4202 of the second adsorption runner 420 is for fresh air or outside air to enter ( As shown in FIG. 11), the cooling area 4202 of the second adsorption rotor 120 is provided for cooling by the fresh air or outside air. In another second embodiment, the first clean gas discharge line 412 is provided with a first clean gas second communication line 485, and the other end of the first clean gas second communication line 485 is connected to the first The second cooling gas inlet line 422 is connected (as shown in FIG. 12) so that the gas in the first clean gas discharge line 412 can be sent to the first through the first clean gas second communication line 485 The cooling zone 4202 of the two adsorption runners 420 is used for cooling. In addition, the first clean gas second communication line 485 is provided with a first clean gas second communication control valve 4851 (as shown in FIG. 12) to control The air volume of the first clean air second communication line 485.

另該一第二脫附濃縮氣體管路425的一端係與該第二吸附轉輪420之脫附區4203的一側A連接，而該第二脫附濃縮氣體管路425的另一端係與一焚燒裝置400連接(如第11圖及第12圖所示)，其中該焚燒裝置400係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第四種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置400乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置400不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置400為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口401及出口402，而該入口401係與該第二脫附濃縮氣體管路425連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該第二脫附濃縮氣體管路 425來輸送到該蓄熱式焚燒爐(RTO)之入口401，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口402則連接至該煙囪470(如第11圖及第12圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪470來排出，另該第二脫附濃縮氣體管路425係設有一風機4251，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口401內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the second desorption concentrated gas line 425 is connected to one side A of the desorption zone 4203 of the second adsorption runner 420, and the other end of the second desorption concentrated gas line 425 is connected to An incineration device 400 is connected (as shown in Figure 11 and Figure 12), wherein the incineration device 400 is a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative type Any one of the incinerators (RTO), and the illustration of the fourth implementation structure of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 400 described below is a regenerative incinerator (RTO) However, the incinerator 400 of the present invention is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 400 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 401 and an outlet 402, and the inlet 401 is connected to the second desorption concentrated gas pipeline 425 , So that the desorbed concentrated gas desorbed by high temperature can pass through the second desorbed concentrated gas pipeline 425 to the inlet 401 of the regenerative incinerator (RTO), so that the desorbed concentrated gas can enter the regenerative incinerator (RTO) for high-temperature cracking to reduce volatile organic compounds, and the regenerative incinerator (RTO) outlet 402 is connected to the chimney 470 (as shown in Figures 11 and 12), so that the clean gas after high-temperature cracking of organic matter can be discharged from the chimney 470, and the second desorption concentration The gas pipeline 425 is provided with a fan 4251 to push and pull the desorbed concentrated gas into the inlet 401 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to undergo high-temperature cracking.

而本發明第四種實施架構(如第11圖及第12圖所示)中主要在於該第二吸附轉輪420除了設有吸附區4201、冷卻區4202及脫附區4203外，還設有高溫脫附區4204，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該第二吸附轉輪420能恢復其吸附能力，使該第二吸附轉輪420能具有四個區域。而該第二吸附轉輪420之高溫脫附區4204的另一側B係與一第四熱氣輸送管路426的一端連接，且該第四熱氣輸送管路426的另一端係與該第四加熱裝置460連接(如第11圖及第12圖所示)，其中該第四加熱裝置460係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第三熱氣輸送管路424係設有一第三熱氣旁通管路492，該第三熱氣旁通管路492的另一端係與該第四加熱裝置460連接(如第11圖及第12圖所示)，以能將經由該第三加熱裝置450進行加熱或熱交換的高溫熱氣能部分分流，並透過該第三熱氣旁通管路492來輸送到該第四加熱裝置460 內，以將進入該第四熱氣輸送管路426內的高溫熱氣能提升到一定溫度(例如300℃)，並將第四熱氣輸送管路426內的高溫熱氣再輸送到該第二吸附轉輪420之高溫脫附區4204，以供進行高溫脫附使用，另該第三熱氣旁通管路492係設有一第三熱氣旁通控制閥門4921(如第12圖所示)，以控制該第三熱氣旁通管路492的風量。 The fourth implementation structure of the present invention (as shown in FIG. 11 and FIG. 12) mainly lies in that the second adsorption rotor 420 is provided with an adsorption zone 4201, a cooling zone 4202 and a desorption zone 4203, as well as The high-temperature desorption zone 4204 can be used to remove residual high-boiling organic compounds (VOC) during online operation (ON LINE), so that the second adsorption runner 420 can restore its adsorption capacity, so that the second adsorption The runner 420 can have four areas. The other side B of the high temperature desorption zone 4204 of the second adsorption runner 420 is connected to one end of a fourth hot gas delivery line 426, and the other end of the fourth hot gas delivery line 426 is connected to the fourth The heating device 460 is connected (as shown in FIGS. 11 and 12), wherein the fourth heating device 460 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is It is any one of an electric heating wire, an electric heating tube or an electric heating sheet, and the pipeline heater (not shown in the figure) is any one using gas fuel or liquid fuel. The third hot gas delivery line 424 is provided with a third hot gas bypass line 492, and the other end of the third hot gas bypass line 492 is connected to the fourth heating device 460 (as shown in FIGS. 11 and 12 (Shown in the figure), so that the high-temperature hot gas that can be heated or exchanged through the third heating device 450 can be partially diverted and sent to the fourth heating device 460 through the third hot gas bypass line 492 In order to raise the high-temperature hot gas entering the fourth hot gas delivery line 426 to a certain temperature (for example, 300°C), and then transport the high-temperature hot gas in the fourth hot gas delivery line 426 to the second adsorption runner The high temperature desorption zone 4204 of 420 is used for high temperature desorption, and the third hot gas bypass line 492 is provided with a third hot gas bypass control valve 4921 (as shown in FIG. 12) to control the first The air volume of the three-heat gas bypass line 492.

再者，該第二吸附轉輪420之高溫脫附區4204的一側A係連接一第二高溫脫附濃縮氣體管路427(如第11圖及第12圖所示)，而該第二高溫脫附濃縮氣體管路427的另一端係與該第二脫附濃縮氣體管路425連接，以將經過該第二吸附轉輪420之高溫脫附區4204所脫附下來的高溫脫附濃縮氣體能透過該第二高溫脫附濃縮氣體管路427來輸送到該第二脫附濃縮氣體管路425內，再透過該第二脫附濃縮氣體管路425輸送到該蓄熱式焚燒爐(RTO)之入口401，讓高溫脫附濃縮氣體能與該第二脫附濃縮氣體管路425內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, a side A of the high-temperature desorption zone 4204 of the second adsorption runner 420 is connected to a second high-temperature desorption concentrated gas line 427 (as shown in FIGS. 11 and 12), and the second The other end of the high-temperature desorption concentrated gas line 427 is connected to the second desorption concentrated gas line 425 to concentrate the high-temperature desorption concentrated through the high-temperature desorption zone 4204 of the second adsorption runner 420 Gas can be transported into the second desorption concentrated gas line 425 through the second high-temperature desorption concentrated gas line 427, and then transferred to the regenerative incinerator (RTO) through the second desorption concentrated gas line 425 ), the high temperature desorption concentrated gas can enter the regenerative incinerator (RTO) together with the desorption concentrated gas in the second desorption concentrated gas pipeline 425 for high temperature cracking.

另本發明第五種實施方式的具高溫脫附之轉輪方法，主要係設有一吸附轉輪510、一第一加熱裝置520及一第二加熱裝置530，而該吸附轉輪510係設有吸附區5101、冷卻區5102、脫附區5103及高溫脫附區5104，因此，本發明主要在於該吸附轉輪510除了設有吸附區5101、冷卻區5102及脫附區5103外，還設有高溫脫附區5104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該吸附轉輪510能恢復其吸附能力，使該吸附轉輪510能具有四個區域。 In addition, in the fifth embodiment of the present invention, the runner method with high temperature desorption mainly includes an adsorption runner 510, a first heating device 520, and a second heating device 530, and the adsorption runner 510 is provided with The adsorption zone 5101, the cooling zone 5102, the desorption zone 5103, and the high-temperature desorption zone 5104. Therefore, the present invention mainly lies in that the adsorption runner 510 is provided with an adsorption zone 5101, a cooling zone 5102, and a desorption zone 5103. The high-temperature desorption zone 5104 can be used to remove residual high-boiling point organic compounds (VOC) during on-line operation (ON LINE), so that the adsorption rotor 510 can restore its adsorption capacity, so that the adsorption rotor 510 can There are four areas.

而該第五種實施方式的主要步驟(如第13圖所示)係包括：步驟S500輸入待吸附之氣體：該吸附轉輪510之吸附區5101的一側A係由一廢氣進氣管路511來輸入待吸附之氣體，而該吸附轉輪510之吸附區5101的另一側B則透過一淨氣排放管路512來輸送經過吸附後之氣體；透過該吸附轉輪510之吸附區5101的一側A係連接一廢氣進氣管路511(如第14圖及第15圖所示)，以能由該廢氣進氣管路511來輸入待吸附之氣體，而該待吸附之氣體可以為揮發性有機化合物(VOC)、二氧化碳(CO2)、氮氣(N2)、水氣或氧氣(O2)之其中任一或複數組合之一，也可以是其他上述未表述之氣體，而該吸附轉輪510之吸附區5101的另一側B則與該一淨氣排放管路512之一端連接(如第14圖及第15圖所示)，讓該待吸附之氣體經該吸附轉輪510之吸附區5101進行吸附後再由該淨氣排放管路512來輸送經過吸附後之氣體。而完成上述步驟S500後即進行下一步驟S510。 The main steps of the fifth embodiment (as shown in FIG. 13) include: Step S500: Input gas to be adsorbed: Side A of the adsorption area 5101 of the adsorption rotor 510 is composed of an exhaust gas inlet line 511 to input the gas to be adsorbed, and the other side B of the adsorption area 5101 of the adsorption rotor 510 conveys the adsorbed gas through a clean gas discharge line 512; through the adsorption area 5101 of the adsorption rotor 510 One side A is connected to an exhaust gas intake line 511 (as shown in FIGS. 14 and 15), so that the exhaust gas intake line 511 can input the gas to be adsorbed, and the gas to be adsorbed can be It is any one or a combination of volatile organic compounds (VOC), carbon dioxide (CO2), nitrogen (N2), water vapor or oxygen (O2), or other gases that are not described above, and the adsorption transfer The other side B of the adsorption area 5101 of the wheel 510 is connected to one end of the clean gas discharge line 512 (as shown in FIGS. 14 and 15), and the gas to be adsorbed passes through the adsorption rotor 510 After the adsorption zone 5101 performs adsorption, the purified gas discharge pipeline 512 transports the adsorbed gas. After the above step S500 is completed, the next step S510 is performed.

另，下一步進行的步驟S510輸入用來冷卻之氣體：該吸附轉輪510之冷卻區5102的一側A係由一冷卻氣進氣管路513來輸入用來冷卻之氣體，而該吸附轉輪510之冷卻區5102的另一側B則透過一冷卻氣輸送管路514來連接至該第一加熱裝置520，以將經過該吸附轉輪510之冷卻區5102的氣體輸送到該第一加熱裝置520內；該吸附轉輪510之冷卻區5102的一側A係連接一冷卻氣進氣管路513(如第14圖及第15圖所示)，以供用來冷卻之氣體進入該吸附轉輪510之冷卻區5102來進行冷卻使用，而該吸附轉輪510之冷卻區5102的另一側B則連接一冷卻氣輸送管路514(如第14圖 及第15圖所示)，該冷卻氣輸送管路514的另一端係與該第一加熱裝置520連接，使能將經過該吸附轉輪510之冷卻區5102的氣體輸送到該第一加熱裝置520內。 In addition, in the next step S510, the gas used for cooling is input: the side A of the cooling zone 5102 of the adsorption rotor 510 is supplied with a gas for cooling by a cooling gas inlet line 513, and the adsorption is turned The other side B of the cooling zone 5102 of the wheel 510 is connected to the first heating device 520 through a cooling gas delivery line 514 to deliver the gas passing through the cooling zone 5102 of the adsorption rotor 510 to the first heating In the device 520; one side A of the cooling zone 5102 of the adsorption runner 510 is connected to a cooling gas inlet line 513 (as shown in FIGS. 14 and 15) for the gas used for cooling to enter the adsorption rotor The cooling zone 5102 of the wheel 510 is used for cooling, and the other side B of the cooling zone 5102 of the adsorption rotor 510 is connected to a cooling gas delivery line 514 (as shown in FIG. 14 And FIG. 15), the other end of the cooling gas delivery line 514 is connected to the first heating device 520, enabling the gas passing through the cooling zone 5102 of the adsorption runner 510 to be transferred to the first heating device Within 520.

而上述該第一加熱裝置520係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。另上述該吸附轉輪510之冷卻區5102係設有兩種實施態樣，其中第一種實施態樣為該吸附轉輪510之冷卻區5102的一側A所連接的冷卻氣進氣管路513乃是供新鮮空氣或外氣進入(如第14圖所示)，透過該新鮮空氣或外氣來提供該吸附轉輪510之冷卻區5102降溫用。另第二種實施態樣係該廢氣進氣管路511係設有一廢氣連通管路581，而該廢氣連通管路581的另一端係與該冷卻氣進氣管路513連接(如第15圖所示)，以能透過該廢氣連通管路581來將該廢氣進氣管路511內的廢氣輸送到該吸附轉輪510之冷卻區5102以進行降溫使用，另該廢氣連通管路581係設有一廢氣連通控制閥門5811(如第15圖所示)，以控制該廢氣連通管路581的風量。而完成上述步驟S510後即進行下一步驟S520。 The above-mentioned first heating device 520 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the cooling zone 5102 of the adsorption rotor 510 is provided with two implementation forms, the first implementation form is a cooling gas inlet line connected to one side A of the cooling zone 5102 of the adsorption rotor 510 513 is for fresh air or outside air to enter (as shown in FIG. 14), and the cooling area 5102 of the adsorption rotor 510 is provided for cooling by the fresh air or outside air. Another second embodiment is that the exhaust gas intake line 511 is provided with an exhaust gas communication line 581, and the other end of the exhaust gas communication line 581 is connected to the cooling gas intake line 513 (as shown in FIG. 15 (Shown), the exhaust gas in the exhaust gas inlet line 511 can be transmitted to the cooling zone 5102 of the adsorption runner 510 through the exhaust gas communication line 581 for cooling, and the exhaust gas communication line 581 is provided There is an exhaust gas communication control valve 5811 (as shown in FIG. 15) to control the air volume of the exhaust gas communication line 581. After the above step S510 is completed, the next step S520 is performed.

另，下一步進行的步驟S520輸送高溫熱氣進行脫附：該吸附轉輪510之脫附區5103的另一側B係由一第一熱氣輸送管路515來輸送該第一加熱裝置520內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路515係設有一熱氣旁通管路591，透過該熱氣旁通管路591連接至該第二加熱裝置530，而該吸附轉輪510之脫附區 5103的一側A則透過一脫附濃縮氣體管路516來輸送經過脫附後之脫附濃縮氣體；該吸附轉輪510之脫附區5103的另一側B係與該一第一熱氣輸送管路515連接，且該第一熱氣輸送管路515的另一端則與該第一加熱裝置520連接(如第14圖及第15圖所示)，以能將經由該第一加熱裝置520進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路515來輸送到該吸附轉輪510之脫附區5103來進行脫附使用。另該第一熱氣輸送管路515係設有一熱氣旁通管路591，該熱氣旁通管路591的另一端係與該第二加熱裝置530連接(如第14圖及第15圖所示)，以能將經由該第一加熱裝置520進行加熱或熱交換的高溫熱氣能部分分流，並透過該熱氣旁通管路591來輸送到該第二加熱裝置530內，另該吸附轉輪510之脫附區5103的一側A係連接一脫附濃縮氣體管路516的一端(如第14圖及第15圖所示)，以用輸送經過該吸附轉輪510之脫附區5103進行脫附後之脫附濃縮氣體。 In addition, the next step S520 transports high-temperature hot gas for desorption: the other side B of the desorption zone 5103 of the adsorption rotor 510 is transported by the first heating device 520 by a first hot gas delivery pipeline 515 The generated high-temperature hot gas is used for desorption, and the first hot gas delivery line 515 is provided with a hot gas bypass line 591, which is connected to the second heating device 530 through the hot gas bypass line 591, and the adsorption runner 510 Desorption Zone One side A of 5103 transports the desorbed concentrated gas through a desorbed concentrated gas pipeline 516; the other side B of the desorption area 5103 of the adsorption runner 510 is transported with the first hot gas The pipeline 515 is connected, and the other end of the first hot gas delivery pipeline 515 is connected to the first heating device 520 (as shown in FIGS. 14 and 15) so that the first heating device 520 can perform The heated or exchanged high-temperature hot gas is transported to the desorption area 5103 of the adsorption rotor 510 through the first hot gas delivery pipeline 515 for desorption use. In addition, the first hot gas delivery line 515 is provided with a hot gas bypass line 591, and the other end of the hot gas bypass line 591 is connected to the second heating device 530 (as shown in FIGS. 14 and 15) In order to partially shunt the high-temperature hot gas that can be heated or exchanged through the first heating device 520, and be transferred to the second heating device 530 through the hot gas bypass line 591, and the adsorption runner 510 One side A of the desorption zone 5103 is connected to one end of a desorption concentrated gas line 516 (as shown in FIG. 14 and FIG. 15) for desorption by the desorption zone 5103 conveyed through the adsorption runner 510 After that, the concentrated gas is desorbed.

而上述該第二加熱裝置530係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該熱氣旁通管路591係設有一熱氣旁通控制閥門5911(如第15圖所示)，以控制該熱氣旁通管路591的風量，使能將經由該第一加熱裝置520進行加熱或熱交換的高溫熱氣部分分流到該第二加熱裝置530內。而完成上述步驟S520後即進行下一步驟S530。 The above-mentioned second heating device 530 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. In addition, the hot gas bypass line 591 is provided with a hot gas bypass control valve 5911 (as shown in FIG. 15) to control the air volume of the hot gas bypass line 591 to enable the first heating device 520 to perform The high-temperature hot gas heated or exchanged is partially shunted into the second heating device 530. After the above step S520 is completed, the next step S530 is performed.

另，下一步進行的步驟S530再將高沸點有機物脫出：該吸附轉輪510之高溫脫附區5104的另一側B係由一第二熱氣輸送管 路517來輸送由該第二加熱裝置530內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該吸附轉輪510之高溫脫附區5104的一側A則透過一高溫脫附濃縮氣體管路518來輸送經過脫附後之高溫脫附濃縮氣體至該脫附濃縮氣體管路516內；該吸附轉輪510之高溫脫附區5104的另一側B係與一第二熱氣輸送管路517的一端連接，且該第二熱氣輸送管路517的另一端係與該第二加熱裝置530連接(如第14圖及第15圖所示)，透過該第二加熱裝置530來將進入該第二熱氣輸送管路517內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路517內的高溫熱氣再輸送到該吸附轉輪510之高溫脫附區5104，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該吸附轉輪510能恢復其吸附能力，另該吸附轉輪510之高溫脫附區5104的一側A係連接一高溫脫附濃縮氣體管路518(如第14圖及第15圖所示)，而該高溫脫附濃縮氣體管路518的另一端係與該脫附濃縮氣體管路516連接，以將經過該吸附轉輪510之高溫脫附區5104所脫附下來的高溫脫附濃縮氣體能透過該高溫脫附濃縮氣體管路518來輸送到該脫附濃縮氣體管路516內。 In addition, in the next step S530, high-boiling organics are removed: the other side B of the high-temperature desorption zone 5104 of the adsorption rotor 510 is a second hot gas delivery pipe The path 517 conveys the high-temperature hot gas raised to a certain temperature by the second heating device 530 to remove high-boiling organic compounds (VOC), and the side A of the high-temperature desorption zone 5104 of the adsorption rotor 510 passes through A high temperature desorption concentrated gas pipeline 518 to transport the desorbed concentrated gas after high temperature to the desorption concentrated gas pipeline 516; the other side B of the high temperature desorption zone 5104 of the adsorption runner 510 is One end of a second hot gas delivery pipe 517 is connected, and the other end of the second hot gas delivery pipe 517 is connected to the second heating device 530 (as shown in FIGS. 14 and 15), through the second The heating device 530 can raise the high-temperature hot gas entering the second hot gas delivery pipeline 517 to a certain temperature (for example, 300°C), and then deliver the high-temperature hot gas in the second hot gas transportation pipeline 517 to the adsorption runner 510 The high temperature desorption zone 5104 is used for high temperature desorption. When it is online (ON LINE), it can remove the remaining high boiling point organic compounds (VOC), so that the adsorption rotor 510 can restore its adsorption capacity. In addition, one side A of the high-temperature desorption zone 5104 of the adsorption rotor 510 is connected to a high-temperature desorption concentrated gas pipeline 518 (as shown in FIGS. 14 and 15), and the high-temperature desorption concentrated gas pipeline 518 The other end is connected to the desorption concentrated gas pipeline 516, so that the high-temperature desorption concentrated gas desorbed through the high-temperature desorption zone 5104 of the adsorption runner 510 can pass through the high-temperature desorption concentrated gas pipeline 518 To the degassed concentrated gas line 516.

而上述該脫附濃縮氣體管路516的另一端係與一焚燒裝置500連接(如第14圖及第15圖所示)，其中該焚燒裝置500係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第五種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置500乃是為蓄熱式焚燒爐(RTO)，但本發明的 焚燒裝置500不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置500為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口501及出口502，而該入口501係與該脫附濃縮氣體管路516連接，其中該脫附濃縮氣體管路516另有與該高溫脫附濃縮氣體管路518的另一端連接，以將經過該吸附轉輪510之高溫脫附區5104所脫附下來的高溫脫附濃縮氣體能透過該高溫脫附濃縮氣體管路518來輸送到該脫附濃縮氣體管路516內，使該脫附濃縮氣體管路516內除了經過該吸附轉輪510之脫附區5103所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該脫附濃縮氣體管路516內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口502則連接至一煙囪570(如第14圖及第15圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪570來排出，另該脫附濃縮氣體管路516係設有一風機5161(如第15圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口501內，讓脫附濃縮氣體能進行高溫裂解。 The other end of the desorption concentrated gas pipeline 516 is connected to an incineration device 500 (as shown in FIGS. 14 and 15), wherein the incineration device 500 is a direct combustion incinerator (TO) (Figure Not shown), catalyst furnace (not shown) or regenerative incinerator (RTO), and the illustration of the fifth embodiment of the present invention is based on regenerative incinerator (RTO) as an example, and the following The illustrated incinerator 500 is a regenerative incinerator (RTO), but the present invention The incinerator 500 is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 500 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 501 and an outlet 502, and the inlet 501 is connected to the desorption concentrated gas pipeline 516, wherein The desorption concentrated gas line 516 is additionally connected to the other end of the high-temperature desorption concentrated gas line 518 to desorb the high-temperature desorption concentrated gas passed through the high-temperature desorption zone 5104 of the adsorption runner 510 The high-temperature desorption concentrated gas line 518 is transported into the desorption concentrated gas line 516, so that the desorption concentrated gas line 516 is desorbed except for the desorption area 5103 passing through the adsorption runner 510 The desorption concentrated gas also contains high-temperature desorption concentrated gas, so that the high-temperature desorption concentrated gas can enter the regenerative incinerator (RTO) together with the desorption concentrated gas in the desorption concentrated gas pipeline 516 for high-temperature cracking, In order to reduce volatile organic compounds, the outlet 502 of the regenerative incinerator (RTO) is connected to a chimney 570 (as shown in Figures 14 and 15) to clean the high-temperature cracked organic compounds It can be discharged by the chimney 570, and the desorption concentrated gas pipeline 516 is provided with a fan 5161 (as shown in Fig. 15) to push and pull the desorbed concentrated gas into the regenerative incinerator (RTO) In the inlet 501, the desorbed concentrated gas can be cracked at high temperature.

而本發明第五種實施架構的具高溫脫附之轉輪系統(如第14圖及第15圖所示)，主要係透過一吸附轉輪510、一第一加熱裝置520、一第二加熱裝置530之組合設計，而本發明第五種實施架構的吸附轉輪510係設有吸附區5101、冷卻區5102、脫附區5103及高溫脫附區5104，該吸附轉輪510係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且一廢氣進氣管路511係連接至該吸附轉輪510之吸 附區5101的一側A(如第14圖及第15圖所示)，以使該吸附轉輪510之吸附區5101能吸附該廢氣進氣管路511內的有機物，而該吸附轉輪510之吸附區5101的另一側B係與該一淨氣排放管路512之一端連接，讓該廢氣經該吸附轉輪510之吸附區5101進行吸附有機物後再由該淨氣排放管路512來輸送。 The fifth embodiment of the present invention, a high-temperature desorption rotor system (as shown in Figure 14 and Figure 15), mainly through an adsorption rotor 510, a first heating device 520, a second heating The combined design of the device 530, and the adsorption rotor 510 of the fifth embodiment of the present invention is provided with an adsorption zone 5101, a cooling zone 5102, a desorption zone 5103, and a high temperature desorption zone 5104. The adsorption runner 510 is a zeolite concentration A runner or a concentrating runner of other materials, and an exhaust gas inlet line 511 is connected to the suction of the suction runner 510 A side A of the attachment zone 5101 (as shown in FIGS. 14 and 15), so that the adsorption zone 5101 of the adsorption runner 510 can adsorb organic matter in the exhaust gas intake line 511, and the adsorption runner 510 The other side B of the adsorption zone 5101 is connected to one end of the one clean gas discharge line 512, so that the exhaust gas adsorbs organic matter through the adsorption zone 5101 of the adsorption rotor 510 and then comes from the clean gas discharge line 512 delivery.

另該吸附轉輪510之冷卻區5102的一側A係連接一冷卻氣進氣管路513(如第14圖及第15圖所示)，以供氣體進入該吸附轉輪510之冷卻區5102來進行冷卻使用，而該吸附轉輪510之冷卻區5102的另一側B係連接一冷卻氣輸送管路514(如第14圖及第15圖所示)，該冷卻氣輸送管路514的另一端係與該第一加熱裝置520連接，其中該第一加熱裝置520係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第一熱氣輸送管路515的一端係與該吸附轉輪510之脫附區5103的另一側B連接(如第14圖及第15圖所示)，且該第一熱氣輸送管路515的另一端則與該第一加熱裝置520連接，以能將經由該第一加熱裝置520進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路515來輸送到該吸附轉輪510之脫附區5103來進行脫附使用。 In addition, one side A of the cooling zone 5102 of the adsorption runner 510 is connected to a cooling gas inlet line 513 (as shown in FIGS. 14 and 15) for the gas to enter the cooling zone 5102 of the adsorption runner 510 For cooling, and the other side B of the cooling zone 5102 of the adsorption runner 510 is connected to a cooling gas delivery line 514 (as shown in FIGS. 14 and 15). The other end is connected to the first heating device 520, wherein the first heating device 520 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is an electric heating wire or an electric heater Either a tube or an electric heating plate, the pipe heater (not shown) is either gas fuel or liquid fuel. One end of the first hot gas delivery pipe 515 is connected to the other side B of the desorption area 5103 of the adsorption rotor 510 (as shown in FIGS. 14 and 15), and the first hot gas delivery pipe The other end of the path 515 is connected to the first heating device 520, so that the high-temperature hot gas heated or exchanged by the first heating device 520 can be transported to the adsorption runner 510 through the first hot gas transport line 515 The desorption area 5103 is used for desorption.

而上述該吸附轉輪510之冷卻區5102係設有兩種實施態樣，其中第一種實施態樣為該吸附轉輪510之冷卻區5102的一側A所連接的冷卻氣進氣管路513乃是供新鮮空氣或外氣進入(如第14圖所示)，透過該新鮮空氣或外氣來提供該吸附轉輪510之冷卻區51 02降溫用。另第二種實施態樣係該廢氣進氣管路511係設有一廢氣連通管路581，而該廢氣連通管路581的另一端係與該冷卻氣進氣管路513連接(如第15圖所示)，以能透過該廢氣連通管路581來將該廢氣進氣管路511內的廢氣輸送到該吸附轉輪510之冷卻區5102以進行降溫使用，另該廢氣連通管路581係設有一廢氣連通控制閥門5811(如第15圖所示)，以控制該廢氣連通管路581的風量。 The cooling zone 5102 of the adsorption rotor 510 described above is provided with two implementations, of which the first implementation is the cooling gas inlet line connected to the side A of the cooling zone 5102 of the adsorption rotor 510 513 is for fresh air or outside air to enter (as shown in FIG. 14), and the cooling area 51 of the adsorption runner 510 is provided through the fresh air or outside air 02 For cooling. Another second embodiment is that the exhaust gas intake line 511 is provided with an exhaust gas communication line 581, and the other end of the exhaust gas communication line 581 is connected to the cooling gas intake line 513 (as shown in FIG. 15 (Shown), the exhaust gas in the exhaust gas inlet line 511 can be transmitted to the cooling zone 5102 of the adsorption runner 510 through the exhaust gas communication line 581 for cooling, and the exhaust gas communication line 581 is provided There is an exhaust gas communication control valve 5811 (as shown in FIG. 15) to control the air volume of the exhaust gas communication line 581.

另該一脫附濃縮氣體管路516的一端係與該吸附轉輪510之脫附區5103的一側A連接，而該脫附濃縮氣體管路516的另一端係與一焚燒裝置500連接(如第14圖及第15圖所示)，其中該焚燒裝置500係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第五種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置500乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置500不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置500為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口501及出口502，而該入口501係與該脫附濃縮氣體管路516連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路516來輸送到該蓄熱式焚燒爐(RTO)之入口501，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口502則連接至一煙囪570(如第14圖及第15圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪570來排出，另該脫附濃縮氣體管路516係設有一風機5161，以能將脫附濃縮氣 體來推拉進入該蓄熱式焚燒爐(RTO)之入口501內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the desorption concentrated gas line 516 is connected to one side A of the desorption area 5103 of the adsorption rotor 510, and the other end of the desorption concentrated gas line 516 is connected to an incineration device 500 ( (As shown in Figure 14 and Figure 15), where the incinerator 500 is a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative incinerator (RTO) Any one of them, and the illustration of the fifth implementation structure of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 500 described below is a regenerative incinerator (RTO), but the incineration of the present invention The device 500 is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 500 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 501 and an outlet 502, and the inlet 501 is connected to the desorption concentrated gas pipeline 516 to The desorbed concentrated gas desorbed by high temperature can be transported to the inlet 501 of the regenerative incinerator (RTO) through the desorbed concentrated gas pipeline 516, so that the desorbed concentrated gas can enter the regenerative incinerator ( RTO) high-temperature cracking to reduce volatile organic compounds, and the outlet 502 of the regenerative incinerator (RTO) is connected to a chimney 570 (as shown in Figures 14 and 15) to pass the high temperature The clean gas after cracking the organic matter can be discharged by the chimney 570, and the desorption concentrated gas pipeline 516 is provided with a fan 5161 to enable the desorption concentrated gas The body is pushed and pulled into the inlet 501 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to undergo high-temperature cracking.

而本發明第五種實施架構(如第14圖及第15圖所示)中主要在於該吸附轉輪510除了設有吸附區5101、冷卻區5102及脫附區5103外，還設有高溫脫附區5104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該吸附轉輪510能恢復其吸附能力，使該吸附轉輪510能具有四個區域。而該吸附轉輪510之高溫脫附區5104的另一側B係與一第二熱氣輸送管路517的一端連接，且該第二熱氣輸送管路517的另一端係與該第二加熱裝置530連接(如第14圖及第15圖所示)，其中該第二加熱裝置530係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第一熱氣輸送管路515係設有一熱氣旁通管路591，該熱氣旁通管路591的另一端係與該第二加熱裝置530連接(如第14圖及第15圖所示)，以能將經由該第一加熱裝置520進行加熱或熱交換的高溫熱氣能部分分流，並透過該熱氣旁通管路591來輸送到該第二加熱裝置530內，以將進入該第二熱氣輸送管路517內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路517內的高溫熱氣再輸送到該吸附轉輪510之高溫脫附區5104，以供進行高溫脫附使用，另該熱氣旁通管路591係設有一熱氣旁通控制閥門5911(如第15圖所示)，以控制該熱氣旁通管路591的風量。 The fifth implementation structure of the present invention (as shown in FIG. 14 and FIG. 15) is mainly that the adsorption runner 510 is provided with a high-temperature desorption in addition to an adsorption zone 5101, a cooling zone 5102 and a desorption zone 5103 Attached area 5104 is used to remove residual high-boiling organic compounds (VOC) during on-line operation (ON LINE), so that the adsorption rotor 510 can restore its adsorption capacity, so that the adsorption rotor 510 can have four Areas. The other side B of the high-temperature desorption zone 5104 of the adsorption rotor 510 is connected to one end of a second hot gas delivery pipe 517, and the other end of the second hot gas delivery pipe 517 is connected to the second heating device 530 connection (as shown in Figure 14 and Figure 15), wherein the second heating device 530 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is electric heating Any one of wire, electric heating tube or electric heating sheet, the pipeline heater (not shown) is any of gas fuel or liquid fuel. The first hot gas delivery line 515 is provided with a hot gas bypass line 591, and the other end of the hot gas bypass line 591 is connected to the second heating device 530 (as shown in FIGS. 14 and 15) , So that the high-temperature hot gas that is heated or exchanged through the first heating device 520 can be partially diverted and sent to the second heating device 530 through the hot gas bypass line 591 to enter the second hot gas The high-temperature hot gas in the conveying pipe 517 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the second hot gas conveying pipe 517 is then sent to the high-temperature desorption zone 5104 of the adsorption runner 510 for proceeding. For high temperature desorption, the hot gas bypass line 591 is provided with a hot gas bypass control valve 5911 (as shown in Figure 15) to control the air volume of the hot gas bypass line 591.

再者，該吸附轉輪510之高溫脫附區5104的一側A係連接一高溫脫附濃縮氣體管路518(如第14圖及第15圖所示)，而該高溫脫附濃縮氣體管路518的另一端係與該脫附濃縮氣體管路516連接，以將經過該吸附轉輪510之高溫脫附區5104所脫附下來的高溫脫附濃縮氣體能透過該高溫脫附濃縮氣體管路518來輸送到該脫附濃縮氣體管路516內，再透過該脫附濃縮氣體管路516輸送到該蓄熱式焚燒爐(RTO)之入口501，讓高溫脫附濃縮氣體能與該脫附濃縮氣體管路516內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, a side A of the high-temperature desorption zone 5104 of the adsorption rotor 510 is connected to a high-temperature desorption concentrated gas pipeline 518 (as shown in FIGS. 14 and 15), and the high-temperature desorption concentrated gas pipe The other end of the path 518 is connected to the desorption concentrated gas pipeline 516, so that the high-temperature desorption concentrated gas desorbed through the high-temperature desorption zone 5104 of the adsorption runner 510 can pass through the high-temperature desorption concentrated gas pipe Road 518 to the desorption concentrated gas pipeline 516, and then to the inlet 501 of the regenerative incinerator (RTO) through the desorption concentrated gas pipeline 516, so that the high-temperature desorption concentrated gas can be desorbed with the The desorbed concentrated gas in the concentrated gas line 516 enters the regenerative incinerator (RTO) together for high-temperature cracking.

另本發明第六種實施方式的具高溫脫附之轉輪方法，主要係設有一吸附轉輪610、一第一加熱裝置620及一第二加熱裝置630，而該吸附轉輪610係設有吸附區6101、冷卻區6102、脫附區6103及高溫脫附區6104，因此，本發明主要在於該吸附轉輪610除了設有吸附區6101、冷卻區6102及脫附區6103外，還設有高溫脫附區6104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該吸附轉輪610能恢復其吸附能力，使該吸附轉輪610能具有四個區域。 In addition, the rotor method with high temperature desorption according to the sixth embodiment of the present invention is mainly provided with an adsorption rotor 610, a first heating device 620 and a second heating device 630, and the adsorption rotor 610 is provided with The adsorption zone 6101, the cooling zone 6102, the desorption zone 6103, and the high-temperature desorption zone 6104. Therefore, the present invention mainly lies in that the adsorption runner 610 is provided with an adsorption zone 6101, a cooling zone 6102, and a desorption zone 6103. The high-temperature desorption zone 6104 can be used to remove residual high-boiling organic compounds (VOC) during online operation (ON LINE), so that the adsorption runner 610 can restore its adsorption capacity, so that the adsorption runner 610 can There are four areas.

而該第六種實施方式的主要步驟(如第16圖所示)係包括：步驟S600輸入待吸附之氣體：該吸附轉輪610之吸附區6101的一側A係由一廢氣進氣管路611來輸入待吸附之氣體，而該吸附轉輪610之吸附區6101的另一側B則透過一淨氣排放管路612來輸送經過吸附後之氣體；透過該吸附轉輪610之吸附區6101的一側A係連接一廢氣進氣管路611(如第17圖及第18圖所示)，以能由該廢 氣進氣管路611來輸入待吸附之氣體，而該待吸附之氣體可以為揮發性有機化合物(VOC)、二氧化碳(CO2)、氮氣(N2)、水氣或氧氣(O2)之其中任一或複數組合之一，也可以是其他上述未表述之氣體，而該吸附轉輪610之吸附區6101的另一側B則與該一淨氣排放管路612之一端連接(如第17圖及第18圖所示)，讓該待吸附之氣體經該吸附轉輪610之吸附區6101進行吸附後再由該淨氣排放管路612來輸送經過吸附後之氣體。而完成上述步驟S600後即進行下一步驟S610。 The main steps of the sixth embodiment (as shown in FIG. 16) include: Step S600: input the gas to be adsorbed: the side A of the adsorption zone 6101 of the adsorption rotor 610 is composed of an exhaust gas inlet line 611 to input the gas to be adsorbed, and the other side B of the adsorption area 6101 of the adsorption rotor 610 conveys the adsorbed gas through a clean gas discharge line 612; through the adsorption area 6101 of the adsorption rotor 610 A side of the system is connected to an exhaust gas intake line 611 (as shown in Figure 17 and Figure 18), so that the waste The gas inlet line 611 is used to input the gas to be adsorbed, and the gas to be adsorbed may be any of volatile organic compounds (VOC), carbon dioxide (CO2), nitrogen (N2), water vapor or oxygen (O2) Or one of the plural combinations, or other gas not described above, and the other side B of the adsorption zone 6101 of the adsorption rotor 610 is connected to one end of the one clean gas discharge line 612 (as shown in Figure 17 and (Shown in FIG. 18), after the gas to be adsorbed is adsorbed through the adsorption area 6101 of the adsorption rotor 610, the adsorbed gas is transported by the clean gas discharge line 612. After the above step S600 is completed, the next step S610 is performed.

另，下一步進行的步驟S610輸入用來冷卻之氣體：該吸附轉輪610之冷卻區6102的另一側B係由一冷卻氣進氣管路613來輸入用來冷卻之氣體，而該吸附轉輪610之冷卻區6102的一側A則透過一冷卻氣輸送管路614來連接至該第一加熱裝置620，以將經過該吸附轉輪610之冷卻區6102的氣體輸送到該第一加熱裝置620內；該吸附轉輪610之冷卻區6102的另一側B係連接一冷卻氣進氣管路613(如第17圖及第18圖所示)，以供用來冷卻之氣體進入該吸附轉輪610之冷卻區6102來進行冷卻使用，而該吸附轉輪610之冷卻區6102的一側A則連接一冷卻氣輸送管路614(如第17圖及第18圖所示)，該冷卻氣輸送管路614的另一端係與該第一加熱裝置620連接，使能將經過該吸附轉輪610之冷卻區6102的氣體輸送到該第一加熱裝置620內。 In addition, in the next step S610, the gas used for cooling is input: the other side B of the cooling area 6102 of the adsorption runner 610 is inputted by a cooling gas inlet line 613 for the gas used for cooling, and the adsorption The side A of the cooling zone 6102 of the runner 610 is connected to the first heating device 620 through a cooling gas delivery line 614 to deliver the gas passing through the cooling zone 6102 of the adsorption runner 610 to the first heating In the device 620; the other side B of the cooling zone 6102 of the adsorption runner 610 is connected to a cooling gas inlet line 613 (as shown in FIGS. 17 and 18) for the cooling gas to enter the adsorption The cooling zone 6102 of the runner 610 is used for cooling, and one side A of the cooling zone 6102 of the adsorption runner 610 is connected to a cooling gas delivery line 614 (as shown in FIGS. 17 and 18). The other end of the gas conveying pipeline 614 is connected to the first heating device 620 to enable the gas passing through the cooling zone 6102 of the adsorption rotor 610 to be conveyed into the first heating device 620.

而上述該第一加熱裝置620係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中 任一。另上述該吸附轉輪610之冷卻區6102係設有兩種實施態樣，其中第一種實施態樣為該吸附轉輪610之冷卻區6102的另一側B所連接的冷卻氣進氣管路613乃是供新鮮空氣或外氣進入(如第17圖所示)，透過該新鮮空氣或外氣來提供該吸附轉輪610之冷卻區6102降溫用。另第二種實施態樣係該淨氣排放管路612係設有一淨氣連通管路682，而該淨氣連通管路682的另一端係與該冷卻氣進氣管路613連接(如第18圖所示)，以能透過該淨氣連通管路682來將該淨氣排放管路612內經過該吸附轉輪610之吸附區6101所吸附過後的氣體輸送到該吸附轉輪610之冷卻區6102以進行降溫使用，另該淨氣連通管路682係設有一淨氣連通控制閥門6821(如第18圖所示)，以控制該淨氣連通管路682的風量。而完成上述步驟S610後即進行下一步驟S620。 The above-mentioned first heating device 620 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is one of gas fuel or liquid fuel Either. In addition, the cooling zone 6102 of the adsorption runner 610 is provided with two implementation forms, the first implementation form is a cooling gas inlet pipe connected to the other side B of the cooling zone 6102 of the adsorption runner 610 The path 613 is for fresh air or outside air to enter (as shown in FIG. 17), and the cooling area 6102 of the adsorption rotor 610 is provided for cooling through the fresh air or outside air. Another second embodiment is that the clean gas discharge line 612 is provided with a clean gas communication line 682, and the other end of the clean gas communication line 682 is connected to the cooling gas intake line 613 (as 18)), the gas adsorbed by the adsorption zone 6101 of the adsorption wheel 610 in the purified gas discharge line 612 through the clean gas communication line 682 is transferred to the adsorption wheel 610 for cooling The zone 6102 is used for cooling. In addition, the clean air communication line 682 is provided with a clean air communication control valve 6821 (as shown in FIG. 18) to control the air volume of the clean air communication line 682. After the above step S610 is completed, the next step S620 is performed.

另，下一步進行的步驟S620輸送高溫熱氣進行脫附：該吸附轉輪610之脫附區6103的一側A係由一第一熱氣輸送管路615來輸送該第一加熱裝置620內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路615係設有一熱氣旁通管路691，透過該熱氣旁通管路691連接至該第二加熱裝置630，而該吸附轉輪610之脫附區6103的另一側B則透過一脫附濃縮氣體管路616來輸送經過脫附後之脫附濃縮氣體；該吸附轉輪610之脫附區6103的一側A係與該一第一熱氣輸送管路615連接，且該第一熱氣輸送管路615的另一端則與該第一加熱裝置620連接(如第17圖及第18圖所示)，以能將經由該第一加熱裝置620進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管 路615來輸送到該吸附轉輪610之脫附區6103來進行脫附使用。另該第一熱氣輸送管路615係設有一熱氣旁通管路691，該熱氣旁通管路691的另一端係與該第二加熱裝置630連接(如第17圖及第18圖所示)，以能將經由該第一加熱裝置620進行加熱或熱交換的高溫熱氣能部分分流，並透過該熱氣旁通管路691來輸送到該第二加熱裝置630內，另該吸附轉輪610之脫附區6103的另一側B係連接一脫附濃縮氣體管路616的一端(如第17圖及第18圖所示)，以用輸送經過該吸附轉輪610之脫附區6103進行脫附後之脫附濃縮氣體。 In addition, the next step S620 is to transport high-temperature hot gas for desorption: the side A of the desorption area 6103 of the adsorption runner 610 is transported by the first heating device 620 by a first hot gas transport line 615 Hot gas for desorption, and the first hot gas delivery line 615 is provided with a hot gas bypass line 691, through which the hot gas bypass line 691 is connected to the second heating device 630, and the adsorption runner 610 The other side B of the desorption zone 6103 conveys the desorbed concentrated gas through a desorption concentrated gas line 616; the side A of the desorption zone 6103 of the adsorption runner 610 is connected to the one The first hot gas delivery line 615 is connected, and the other end of the first hot gas delivery line 615 is connected to the first heating device 620 (as shown in FIGS. 17 and 18) so that the first The high-temperature hot gas for heating or heat exchange by the heating device 620 passes through the first hot gas delivery pipe Road 615 is transported to the desorption area 6103 of the adsorption rotor 610 for desorption use. In addition, the first hot gas delivery line 615 is provided with a hot gas bypass line 691, and the other end of the hot gas bypass line 691 is connected to the second heating device 630 (as shown in FIGS. 17 and 18) So that the high-temperature hot gas that is heated or exchanged through the first heating device 620 can be partially diverted and transported into the second heating device 630 through the hot gas bypass line 691, and the adsorption runner 610 can The other side B of the desorption zone 6103 is connected to one end of a desorption concentrated gas pipeline 616 (as shown in FIGS. 17 and 18) for desorption zone 6103 conveyed through the adsorption runner 610 The attached desorbed concentrated gas.

而上述該第二加熱裝置630係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。且上述該熱氣旁通管路691係設有一熱氣旁通控制閥門6911(如第18圖所示)，以控制該熱氣旁通管路691的風量，使能將經由該第一加熱裝置620進行加熱或熱交換的高溫熱氣部分分流到該第二加熱裝置630內。而完成上述步驟S620後即進行下一步驟S630。 The above-mentioned second heating device 630 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is any one of an electric heating wire, an electric heating tube or an electric heating sheet, the piping The heater (not shown) is either gas fuel or liquid fuel. Moreover, the hot gas bypass line 691 is provided with a hot gas bypass control valve 6911 (as shown in FIG. 18) to control the air volume of the hot gas bypass line 691 to enable the first heating device 620 to perform The high-temperature hot gas heated or exchanged is partially shunted into the second heating device 630. After the above step S620 is completed, the next step S630 is performed.

另，下一步進行的步驟S630再將高沸點有機物脫出：該吸附轉輪610之高溫脫附區6104的一側A係由一第二熱氣輸送管路617來輸送由該第二加熱裝置630內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該吸附轉輪610之高溫脫附區6104的另一側B則透過一高溫脫附濃縮氣體管路618來輸送經過脫附後之高溫脫附濃縮氣體至該脫附濃縮氣體管路616內；該吸附轉輪610之高溫脫附區6104的一側A係與一第二熱氣輸送管路617的一端連接， 且該第二熱氣輸送管路617的另一端係與該第二加熱裝置630連接(如第17圖及第18圖所示)，透過該第二加熱裝置630來將進入該第二熱氣輸送管路617內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路617內的高溫熱氣再輸送到該吸附轉輪610之高溫脫附區6104，以供進行高溫脫附使用，當在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該吸附轉輪610能恢復其吸附能力，另該吸附轉輪610之高溫脫附區6104的另一側B係連接一高溫脫附濃縮氣體管路618(如第17圖及第18圖所示)，而該高溫脫附濃縮氣體管路618的另一端係與該脫附濃縮氣體管路616連接，以將經過該吸附轉輪610之高溫脫附區6104所脫附下來的高溫脫附濃縮氣體能透過該高溫脫附濃縮氣體管路618來輸送到該脫附濃縮氣體管路616內。 In addition, the next step S630 is to remove the high-boiling organic matter: the side A of the high-temperature desorption zone 6104 of the adsorption rotor 610 is conveyed by the second heating gas conveying pipeline 617 by the second heating device 630 The high temperature hot gas raised to a certain temperature inside to remove high boiling point organic compounds (VOC), and the other side B of the high temperature desorption zone 6104 of the adsorption rotor 610 is through a high temperature desorption concentrated gas line 618 to The high-temperature desorbed concentrated gas after desorption is transported to the desorbed concentrated gas pipeline 616; the side A of the high-temperature desorption zone 6104 of the adsorption runner 610 is connected to one end of a second hot gas conveying pipeline 617 , And the other end of the second hot gas conveying pipe 617 is connected to the second heating device 630 (as shown in FIGS. 17 and 18), through the second heating device 630 to enter the second hot gas conveying pipe The high-temperature hot gas in the path 617 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the second hot gas delivery pipe 617 is sent to the high-temperature desorption area 6104 of the adsorption runner 610 for high-temperature desorption Attached to use, when online operation (ON LINE), the remaining high boiling point organic compounds (VOC) can be removed, so that the adsorption rotor 610 can restore its adsorption capacity, and the adsorption rotor 610 high temperature desorption zone 6104 The other side B is connected to a high-temperature desorption concentrated gas line 618 (as shown in FIGS. 17 and 18), and the other end of the high-temperature desorption concentrated gas line 618 is connected to the desorption concentrated gas tube Road 616 is connected so that the high-temperature desorption concentrated gas desorbed through the high-temperature desorption zone 6104 of the adsorption runner 610 can be transported to the desorption concentrated gas pipeline 616 through the high-temperature desorption concentrated gas pipeline 618 Inside.

而上述該脫附濃縮氣體管路616的另一端係與一焚燒裝置600連接(如第17圖及第18圖所示)，其中該焚燒裝置600係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第六種實施方式之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置600乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置600不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置600為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口601及出口602，而該入口601係與該脫附濃縮氣體管路616連接，其中該脫附濃縮氣體管路616另有與該高溫脫附濃縮氣體管路618的另一端連接，以將經過該 吸附轉輪610之高溫脫附區6104所脫附下來的高溫脫附濃縮氣體能透過該高溫脫附濃縮氣體管路618來輸送到該脫附濃縮氣體管路616內，使該脫附濃縮氣體管路616內除了經過該吸附轉輪610之脫附區6103所脫附下來的脫附濃縮氣體外還含有高溫脫附濃縮氣體，讓高溫脫附濃縮氣體能與該脫附濃縮氣體管路616內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口602則連接至一煙囪670(如第17圖及第18圖所示)，以將經過高溫裂解有機化合物後的乾淨氣體能由該煙囪670來排出，另該脫附濃縮氣體管路616係設有一風機6161(如第18圖所示)，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口601內，讓脫附濃縮氣體能進行高溫裂解。 The other end of the desorption concentrated gas pipeline 616 is connected to an incinerator 600 (as shown in FIGS. 17 and 18), wherein the incinerator 600 is a direct combustion incinerator (TO) (Figure (Not shown), catalyst furnace (not shown), or regenerative incinerator (RTO), and the illustration of the sixth embodiment of the present invention takes the regenerative incinerator (RTO) as an example, and the following The illustrated incinerator 600 is a regenerative incinerator (RTO), but the incinerator 600 of the present invention is not limited to a regenerative incinerator (RTO), but may also be a direct combustion incinerator (TO) (not shown) ) Or catalyst furnace (not shown). When the incinerator 600 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 601 and an outlet 602, and the inlet 601 is connected to the desorption concentrated gas pipeline 616, wherein The desorption concentrated gas line 616 is additionally connected to the other end of the high-temperature desorption concentrated gas line 618 to pass the The high-temperature desorption concentrated gas desorbed by the high-temperature desorption zone 6104 of the adsorption runner 610 can be transported into the desorption concentrated gas pipeline 616 through the high-temperature desorption concentrated gas pipeline 618 to make the desorbed concentrated gas The pipeline 616 contains high-temperature desorption concentrated gas in addition to the desorption concentrated gas desorbed through the desorption zone 6103 of the adsorption runner 610, so that the high-temperature desorption concentrated gas can communicate with the desorption concentrated gas pipeline 616 The desorbed concentrated gas inside enters into the regenerative incinerator (RTO) for high temperature cracking to reduce volatile organic compounds, and the outlet 602 of the regenerative incinerator (RTO) is connected to a chimney 670 (such as the Figure 17 and Figure 18), so that the clean gas after high-temperature cracking of organic compounds can be discharged by the chimney 670, and the desorption concentrated gas pipeline 616 is provided with a fan 6161 (as shown in Figure 18) ), so that the desorbed concentrated gas can be pushed and pulled into the inlet 601 of the regenerative incinerator (RTO) to allow the desorbed concentrated gas to undergo high-temperature cracking.

而本發明第六種實施架構的具高溫脫附之轉輪系統(如第17圖及第18圖所示)，主要係透過一吸附轉輪610、一第一加熱裝置620、一第二加熱裝置630之組合設計，而本發明第六種實施架構的吸附轉輪610係設有吸附區6101、冷卻區6102、脫附區6103及高溫脫附區6104，該吸附轉輪610係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且一廢氣進氣管路611係連接至該吸附轉輪610之吸附區6101的一側A(如第17圖及第18圖所示)，以使該吸附轉輪610之吸附區6101能吸附該廢氣進氣管路611內的有機物，而該吸附轉輪610之吸附區6101的另一側B係與該一淨氣排放管路612之一端連接，讓該廢氣經該吸附轉輪610之吸附區6101進行吸附有機物後再由該淨氣排放管路612來輸送。 The runner system with high temperature desorption according to the sixth embodiment of the present invention (as shown in FIGS. 17 and 18) is mainly through an adsorption runner 610, a first heating device 620, and a second heating The combination design of the device 630, and the adsorption rotor 610 of the sixth embodiment of the present invention is provided with an adsorption zone 6101, a cooling zone 6102, a desorption zone 6103, and a high-temperature desorption zone 6104. The adsorption runner 610 is a zeolite concentration A runner or a concentrating runner of other materials, and an exhaust gas inlet line 611 is connected to the side A (as shown in FIGS. 17 and 18) of the adsorption zone 6101 of the adsorption runner 610, so that The adsorption area 6101 of the adsorption rotor 610 can adsorb organic matter in the exhaust gas inlet line 611, and the other side B of the adsorption area 6101 of the adsorption rotor 610 is connected to one end of the one clean gas discharge line 612 After the exhaust gas passes through the adsorption zone 6101 of the adsorption rotor 610 to adsorb organic substances, the exhaust gas is sent through the clean gas discharge line 612.

另該吸附轉輪610之冷卻區6102的另一側B係連接一冷卻氣進氣管路613(如第17圖及第18圖所示)，以供氣體進入該吸附轉輪610之冷卻區6102來進行冷卻使用，而該吸附轉輪610之冷卻區6102的一側A係連接一冷卻氣輸送管路614(如第17圖及第18圖所示)，該冷卻氣輸送管路614的另一端係與該第一加熱裝置620連接，其中該第一加熱裝置620係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該一第一熱氣輸送管路615的一端係與該吸附轉輪610之脫附區6103的一側A連接(如第17圖及第18圖所示)，且該第一熱氣輸送管路615的另一端則與該第一加熱裝置620連接，以能將經由該第一加熱裝置620進行加熱或熱交換的高溫熱氣透過該第一熱氣輸送管路615來輸送到該吸附轉輪610之脫附區6103來進行脫附使用。 In addition, the other side B of the cooling zone 6102 of the adsorption runner 610 is connected to a cooling gas inlet line 613 (as shown in FIGS. 17 and 18) for the gas to enter the cooling zone of the adsorption runner 610 6102 for cooling, and a side A of the cooling zone 6102 of the adsorption runner 610 is connected to a cooling gas delivery line 614 (as shown in FIGS. 17 and 18). The other end is connected to the first heating device 620, wherein the first heating device 620 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is an electric heating wire or an electric heater Either a tube or an electric heating plate, the pipe heater (not shown) is either gas fuel or liquid fuel. One end of the first hot gas delivery pipe 615 is connected to one side A of the desorption area 6103 of the adsorption rotor 610 (as shown in FIGS. 17 and 18), and the first hot gas delivery pipe The other end of 615 is connected to the first heating device 620, so that the high-temperature hot gas heated or exchanged by the first heating device 620 can be transported to the adsorption runner 610 through the first hot gas delivery pipe 615 The desorption area 6103 is used for desorption.

而上述該吸附轉輪610之冷卻區6102係設有兩種實施態樣，其中第一種實施態樣為該吸附轉輪610之冷卻區6102的另一側B所連接的冷卻氣進氣管路613乃是供新鮮空氣或外氣進入(如第17圖所示)，透過該新鮮空氣或外氣來提供該吸附轉輪610之冷卻區6102降溫用。另第二種實施態樣係該淨氣排放管路612係設有一淨氣連通管路682，而該淨氣連通管路682的另一端係與該冷卻氣進氣管路613連接(如第18圖所示)，以能透過該淨氣連通管路682來將該淨氣排放管路612內經過該吸附轉輪610之吸附區6101所吸附過後的氣體輸送到該吸附轉輪610之冷卻區6102以進行降溫使用， 另該淨氣連通管路682係設有一淨氣連通控制閥門6821(如第18圖所示)，以控制該淨氣連通管路682的風量。 The cooling zone 6102 of the adsorption rotor 610 is provided with two implementation forms, the first implementation form is a cooling gas inlet pipe connected to the other side B of the cooling zone 6102 of the adsorption rotor 610 The path 613 is for fresh air or outside air to enter (as shown in FIG. 17), and the cooling area 6102 of the adsorption rotor 610 is provided for cooling through the fresh air or outside air. Another second embodiment is that the clean gas discharge line 612 is provided with a clean gas communication line 682, and the other end of the clean gas communication line 682 is connected to the cooling gas intake line 613 (as 18)), the gas adsorbed by the adsorption zone 6101 of the adsorption wheel 610 in the purified gas discharge line 612 through the clean gas communication line 682 is transferred to the adsorption wheel 610 for cooling Zone 6102 for cooling use, In addition, the clean air communication line 682 is provided with a clean air communication control valve 6821 (as shown in FIG. 18) to control the air volume of the clean air communication line 682.

另該一脫附濃縮氣體管路616的一端係與該吸附轉輪610之脫附區6103的另一側B連接，而該脫附濃縮氣體管路616的另一端係與一焚燒裝置600連接(如第17圖及第18圖所示)，其中該焚燒裝置600係為直燃式焚燒爐(TO)(圖未示)、觸媒爐(圖未示)或蓄熱式焚燒爐(RTO)之其中任一，而本發明第六種實施架構之圖示係以蓄熱式焚燒爐(RTO)為例，且下面說明的焚燒裝置600乃是為蓄熱式焚燒爐(RTO)，但本發明的焚燒裝置600不以蓄熱式焚燒爐(RTO)為限，也可以是直燃式焚燒爐(TO)(圖未示)或觸媒爐(圖未示)。而當該焚燒裝置600為蓄熱式焚燒爐(RTO)時，該蓄熱式焚燒爐(RTO)係設有入口601及出口602，而該入口601係與該脫附濃縮氣體管路616連接，以能將經過高溫所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路616來輸送到該蓄熱式焚燒爐(RTO)之入口601，讓脫附濃縮氣體能進入該蓄熱式焚燒爐(RTO)內進行高溫裂解，以能減少揮發性有機化合物，另該蓄熱式焚燒爐(RTO)之出口602則連接至一煙囪670(如第17圖及第18圖所示)，以將經過高溫裂解有機物後的乾淨氣體能由該煙囪670來排出，另該脫附濃縮氣體管路616係設有一風機6161，以能將脫附濃縮氣體來推拉進入該蓄熱式焚燒爐(RTO)之入口601內，讓脫附濃縮氣體能進行高溫裂解。 Another end of the desorption concentrated gas pipeline 616 is connected to the other side B of the desorption zone 6103 of the adsorption rotor 610, and the other end of the desorption concentrated gas pipeline 616 is connected to an incinerator 600 (As shown in Figure 17 and Figure 18), wherein the incinerator 600 is a direct combustion incinerator (TO) (not shown), a catalyst furnace (not shown) or a regenerative incinerator (RTO) Any one of them, and the illustration of the sixth embodiment of the present invention takes the regenerative incinerator (RTO) as an example, and the incinerator 600 described below is a regenerative incinerator (RTO), but the present invention The incinerator 600 is not limited to a regenerative incinerator (RTO), and may also be a direct combustion incinerator (TO) (not shown) or a catalyst furnace (not shown). When the incinerator 600 is a regenerative incinerator (RTO), the regenerative incinerator (RTO) is provided with an inlet 601 and an outlet 602, and the inlet 601 is connected to the desorption concentrated gas pipeline 616 to The desorbed concentrated gas desorbed by high temperature can be transported to the inlet 601 of the regenerative incinerator (RTO) through the desorbed concentrated gas pipeline 616, so that the desorbed concentrated gas can enter the regenerative incinerator ( RTO) high-temperature cracking to reduce volatile organic compounds, and the outlet 602 of the regenerative incinerator (RTO) is connected to a chimney 670 (as shown in Figure 17 and Figure 18) to pass the high temperature The clean gas after cracking organic matter can be discharged by the chimney 670, and the desorption concentrated gas pipeline 616 is provided with a fan 6161 to push and pull the desorbed concentrated gas into the inlet 601 of the regenerative incinerator (RTO) Inside, the desorption concentrated gas can be cracked at high temperature.

而本發明第六種實施架構(如第17圖及第18圖所示)中主要在於該吸附轉輪610除了設有吸附區6101、冷卻區6102及 脫附區6103外，還設有高溫脫附區6104，以用來在線運轉(ON LINE)時，能將所殘留的高沸點有機物(VOC)脫出，讓該吸附轉輪610能恢復其吸附能力，使該吸附轉輪610能具有四個區域。而該吸附轉輪610之高溫脫附區6104的一側A係與一第二熱氣輸送管路617的一端連接，且該第二熱氣輸送管路617的另一端係與該第二加熱裝置630連接(如第17圖及第18圖所示)，其中該第二加熱裝置630係為加熱器、管道加熱器或熱交換器之其中任一，該加熱器(圖未示)係為電熱絲、電熱管或電熱片之其中任一，該管道加熱器(圖未示)係為採用氣體燃料或液體燃料之其中任一。而該第一熱氣輸送管路615係設有一熱氣旁通管路691，該熱氣旁通管路691的另一端係與該第二加熱裝置630連接(如第17圖及第18圖所示)，以能將經由該第一加熱裝置620進行加熱或熱交換的高溫熱氣能部分分流，並透過該熱氣旁通管路691來輸送到該第二加熱裝置630內，以將進入該第二熱氣輸送管路617內的高溫熱氣能提升到一定溫度(例如300℃)，並將第二熱氣輸送管路617內的高溫熱氣再輸送到該吸附轉輪610之高溫脫附區6104，以供進行高溫脫附使用，另該熱氣旁通管路691係設有一熱氣旁通控制閥門6911(如第18圖所示)，以控制該熱氣旁通管路691的風量。 The sixth implementation structure of the present invention (as shown in FIGS. 17 and 18) mainly lies in that the adsorption rotor 610 is provided with an adsorption zone 6101, a cooling zone 6102 and In addition to the desorption zone 6103, there is also a high-temperature desorption zone 6104, which can be used to remove the remaining high-boiling organic compounds (VOC) during online operation (ON LINE), so that the adsorption runner 610 can resume its adsorption The ability to enable the suction runner 610 to have four regions. One side A of the high-temperature desorption zone 6104 of the adsorption rotor 610 is connected to one end of a second hot gas delivery pipe 617, and the other end of the second hot gas delivery pipe 617 is connected to the second heating device 630 Connection (as shown in Figure 17 and Figure 18), wherein the second heating device 630 is any one of a heater, a pipe heater or a heat exchanger, and the heater (not shown) is an electric heating wire , Electric heating tube or electric heating plate, the pipeline heater (not shown) is any one of gas fuel or liquid fuel. The first hot gas delivery line 615 is provided with a hot gas bypass line 691, and the other end of the hot gas bypass line 691 is connected to the second heating device 630 (as shown in FIGS. 17 and 18) So that the high-temperature hot gas that is heated or exchanged through the first heating device 620 can be partially diverted and sent to the second heating device 630 through the hot gas bypass line 691 to enter the second hot gas The high-temperature hot gas in the conveying pipe 617 can be raised to a certain temperature (for example, 300°C), and the high-temperature hot gas in the second hot gas conveying pipe 617 is then sent to the high-temperature desorption zone 6104 of the adsorption runner 610 for proceeding. For high temperature desorption, the hot gas bypass line 691 is provided with a hot gas bypass control valve 6911 (as shown in Fig. 18) to control the air volume of the hot gas bypass line 691.

再者，該吸附轉輪610之高溫脫附區6104的另一側B係連接一高溫脫附濃縮氣體管路618(如第17圖及第18圖所示)，而該高溫脫附濃縮氣體管路618的另一端係與該脫附濃縮氣體管路616連接，以將經過該吸附轉輪610之高溫脫附區6104所脫附下來的 高溫脫附濃縮氣體能透過該高溫脫附濃縮氣體管路618來輸送到該脫附濃縮氣體管路616內，再透過該脫附濃縮氣體管路616輸送到該蓄熱式焚燒爐(RTO)之入口601，讓高溫脫附濃縮氣體能與該脫附濃縮氣體管路616內的脫附濃縮氣體一起進入該蓄熱式焚燒爐(RTO)內進行高溫裂解。 Furthermore, the other side B of the high temperature desorption zone 6104 of the adsorption runner 610 is connected to a high temperature desorption concentrated gas pipeline 618 (as shown in FIGS. 17 and 18), and the high temperature desorption concentrated gas The other end of the pipeline 618 is connected to the desorption concentrated gas pipeline 616 to desorb the high-temperature desorption zone 6104 passing through the adsorption runner 610 The high-temperature desorption concentrated gas can be transferred into the desorption concentrated gas line 616 through the high-temperature desorption concentrated gas line 618, and then transferred to the regenerative incinerator (RTO) through the desorption concentrated gas line 616 The inlet 601 allows the high-temperature desorption concentrated gas to enter the regenerative incinerator (RTO) together with the desorption concentrated gas in the desorption concentrated gas pipeline 616 for high-temperature cracking.

由以上詳細說明，可使熟知本項技藝者明瞭本發明的確可達成前述目的，實已符合專利法之規定，爰提出發明專利申請。 From the above detailed description, those who are familiar with this skill can understand that the present invention can indeed achieve the aforementioned objectives, and in fact have complied with the provisions of the Patent Law, and filed an application for an invention patent.

惟以上所述者，僅為本發明之較佳實施例而已，當不能以此限定本發明實施之範圍；故，凡依本發明申請專利範圍及發明說明書內容所作之簡單的等效變化與修飾，皆應仍屬本發明專利涵蓋之範圍內。 However, the above are only preferred embodiments of the present invention, which should not be used to limit the scope of implementation of the present invention; therefore, simple equivalent changes and modifications made according to the scope of the patent application of the present invention and the content of the invention description , Should still fall within the scope of this invention patent.

A‧‧‧一側 A‧‧‧side

B‧‧‧另一側 B‧‧‧The other side

100‧‧‧焚燒裝置 100‧‧‧Incinerator

101‧‧‧入口 101‧‧‧ entrance

102‧‧‧出口 102‧‧‧Export

110‧‧‧第一吸附轉輪 110‧‧‧The first adsorption runner

1101‧‧‧吸附區 1101‧‧‧Adsorption zone

1102‧‧‧冷卻區 1102‧‧‧cooling zone

1103‧‧‧脫附區 1103‧‧‧Desorption zone

1104‧‧‧高溫脫附區 1104‧‧‧High temperature desorption zone

111‧‧‧廢氣進氣管路 111‧‧‧ Exhaust gas inlet line

112‧‧‧第一淨氣排放管路 112‧‧‧The first clean gas discharge line

113‧‧‧第一冷卻氣進氣管路 113‧‧‧The first cooling air intake line

114‧‧‧第一冷卻氣輸送管路 114‧‧‧ First cooling gas delivery pipeline

115‧‧‧第一熱氣輸送管路 115‧‧‧The first hot gas delivery pipeline

116‧‧‧第一脫附濃縮氣體管路 116‧‧‧The first desorption concentrated gas pipeline

117‧‧‧第二熱氣輸送管路 117‧‧‧Second hot gas delivery pipeline

118‧‧‧第一高溫脫附濃縮氣體管路 118‧‧‧The first high temperature desorption concentrated gas pipeline

120‧‧‧第二吸附轉輪 120‧‧‧Second adsorption runner

1201‧‧‧吸附區 1201‧‧‧Adsorption zone

1202‧‧‧冷卻區 1202‧‧‧cooling area

1203‧‧‧脫附區 1203‧‧‧Desorption zone

1204‧‧‧高溫脫附區 1204‧‧‧High temperature desorption zone

121‧‧‧第二淨氣排放管路 121‧‧‧Second clean gas discharge line

122‧‧‧第二冷卻氣進氣管路 122‧‧‧Second cooling air intake line

123‧‧‧第二冷卻氣輸送管路 123‧‧‧ Second cooling gas delivery pipeline

124‧‧‧第三熱氣輸送管路 124‧‧‧The third hot gas delivery pipeline

125‧‧‧第二脫附濃縮氣體管路 125‧‧‧Second desorption concentrated gas pipeline

126‧‧‧第四熱氣輸送管路 126‧‧‧The fourth hot gas delivery pipeline

127‧‧‧第二高溫脫附濃縮氣體管路 127‧‧‧Second high-temperature desorption concentrated gas pipeline

130‧‧‧第一加熱裝置 130‧‧‧First heating device

140‧‧‧第二加熱裝置 140‧‧‧Second heating device

150‧‧‧第三加熱裝置 150‧‧‧The third heating device

160‧‧‧第四加熱裝置 160‧‧‧The fourth heating device

170‧‧‧煙囪 170‧‧‧Chimney

191‧‧‧第一熱氣旁通管路 191‧‧‧The first hot gas bypass line

192‧‧‧第三熱氣旁通管路 192‧‧‧The third hot gas bypass line

Claims (64)

一種具高溫脫附之轉輪方法，係設有一第一吸附轉輪、一第二吸附轉輪、一第一加熱裝置、一第二加熱裝置、一第三加熱裝置及一第四加熱裝置，該轉輪方法的主要步驟係包括；輸入待吸附之氣體：該第一吸附轉輪之吸附區的一側係由一廢氣進氣管路來輸入待吸附之氣體，而該第一吸附轉輪之吸附區的另一側則透過一第一淨氣排放管路來輸送經過吸附後之氣體；輸入用來冷卻之氣體：該第一吸附轉輪之冷卻區的一側係由一第一冷卻氣進氣管路來輸入用來冷卻之氣體，而該第一吸附轉輪之冷卻區的另一側則透過一第一冷卻氣輸送管路來連接至該第一加熱裝置，以將經過該第一吸附轉輪之冷卻區的氣體輸送到該第一加熱裝置內；輸送高溫熱氣進行脫附：該第一吸附轉輪之脫附區的另一側係由一第一熱氣輸送管路來輸送該第一加熱裝置內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路係設有一第一熱氣旁通管路，透過該第一熱氣旁通管路連接至該第二加熱裝置，而該第一吸附轉輪之脫附區的一側則透過一第一脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；再將高沸點有機物脫出：該第一吸附轉輪之高溫脫附區的另一側係由一第二熱氣輸送管路來輸送由該第二加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪之高溫脫附區的一側則透過一第一高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路內；輸送欲再吸附之氣體：該第二吸附轉輪之吸附區的一側係由該第一淨氣 排放管路來輸送欲進行再吸附之氣體，而該第二吸附轉輪之吸附區的另一側則透過一第二淨氣排放管路來輸送經過再吸附後之氣體；輸入用來冷卻之氣體：該第二吸附轉輪之冷卻區的一側係由一第二冷卻氣進氣管路來輸入用來冷卻之氣體，而該第二吸附轉輪之冷卻區的另一側則透過一第二冷卻氣輸送管路來連接至該第三加熱裝置，以將經過該第二吸附轉輪之冷卻區的氣體輸送到該第三加熱裝置內；輸送高溫熱氣進行脫附：該第二吸附轉輪之脫附區的另一側係由一第三熱氣輸送管路來輸送該第三加熱裝置內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路係設有一第三熱氣旁通管路，透過該第三熱氣旁通管路連接至該第四加熱裝置，而該第二吸附轉輪之脫附區的一側則透過一第二脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；以及再將高沸點有機物脫出：該第二吸附轉輪之高溫脫附區的另一側係由一第四熱氣輸送管路來輸送由該第四加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪之高溫脫附區的一側則透過一第二高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路內。 A runner method with high temperature desorption is provided with a first adsorption runner, a second adsorption runner, a first heating device, a second heating device, a third heating device and a fourth heating device, The main steps of the runner method include: input of gas to be adsorbed: one side of the adsorption area of the first adsorption runner is inputted by a waste gas inlet line, and the first adsorption runner The other side of the adsorption zone transports the gas after adsorption through a first clean gas discharge line; input gas for cooling: one side of the cooling zone of the first adsorption runner is cooled by a first The gas inlet line is used to input the gas for cooling, and the other side of the cooling area of the first adsorption runner is connected to the first heating device through a first cooling gas delivery line to pass through the The gas in the cooling zone of the first adsorption runner is delivered to the first heating device; high-temperature hot gas is delivered for desorption: the other side of the desorption zone of the first adsorption runner is provided by a first hot gas delivery pipeline The high-temperature hot gas generated in the first heating device is conveyed for desorption, and the first hot gas conveying pipeline is provided with a first hot gas bypass pipeline connected to the second through the first hot gas bypass pipeline Heating device, and one side of the desorption zone of the first adsorption runner conveys the desorbed concentrated gas after desorption through a first desorbed concentrated gas pipeline; then the high-boiling organic matter is removed: the first The other side of the high-temperature desorption zone of an adsorption runner is transported by a second hot gas delivery pipeline to transport high-temperature hot gas raised to a certain temperature in the second heating device to remove high-boiling organics (VOC) , And one side of the high-temperature desorption zone of the first adsorption runner conveys the high-temperature desorption concentrated gas after desorption to the first desorption concentrated gas pipeline through a first high-temperature desorption concentrated gas pipeline Inside; transport the gas to be re-adsorbed: the side of the adsorption area of the second adsorption runner is controlled by the first clean gas The discharge pipe conveys the gas to be re-adsorbed, and the other side of the adsorption area of the second adsorption runner transfers the re-adsorbed gas through a second clean gas discharge pipe; input for cooling Gas: One side of the cooling zone of the second adsorption runner is supplied with gas for cooling by a second cooling gas inlet line, while the other side of the cooling zone of the second adsorption runner passes through a The second cooling gas delivery line is connected to the third heating device to deliver the gas passing through the cooling area of the second adsorption runner to the third heating device; delivering high temperature hot gas for desorption: the second adsorption On the other side of the desorption zone of the runner, a third hot gas conveying pipeline is used to convey the high-temperature hot gas generated in the third heating device for desorption, and the third hot gas conveying pipeline is provided with a third The hot gas bypass line is connected to the fourth heating device through the third hot gas bypass line, and one side of the desorption zone of the second adsorption runner is conveyed through a second desorption concentrated gas line The desorbed concentrated gas after desorption; and the high-boiling organics are removed again: the other side of the high-temperature desorption zone of the second adsorption runner is conveyed by a fourth hot gas conveying pipeline by the fourth heating The high temperature hot gas raised to a certain temperature in the device to remove high boiling point organic compounds (VOC), and the side of the high temperature desorption zone of the second adsorption runner is through a second high temperature desorption concentrated gas pipeline to The high-temperature desorption concentrated gas after desorption is delivered to the second desorption concentrated gas pipeline. 一種具高溫脫附之轉輪方法，係設有一第一吸附轉輪、一第二吸附轉輪、一第一加熱裝置、一第二加熱裝置、一第三加熱裝置及一第四加熱裝置，該轉輪方法的主要步驟係包括；輸入待吸附之氣體：該第一吸附轉輪之吸附區的一側係由一廢氣進氣管路來輸入待吸附之氣體，而該第一吸附轉輪之吸附區的另一側則透過一 第一淨氣排放管路來輸送經過吸附後之氣體；輸入用來冷卻之氣體：該第一吸附轉輪之冷卻區的另一側係由一第一冷卻氣進氣管路來輸入用來冷卻之氣體，而該第一吸附轉輪之冷卻區的一側則透過一第一冷卻氣輸送管路來連接至該第一加熱裝置，以將經過該第一吸附轉輪之冷卻區的氣體輸送到該第一加熱裝置內；輸送高溫熱氣進行脫附：該第一吸附轉輪之脫附區的一側係由一第一熱氣輸送管路來輸送該第一加熱裝置內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路係設有一第一熱氣旁通管路，透過該第一熱氣旁通管路連接至該第二加熱裝置，而該第一吸附轉輪之脫附區的另一側則透過一第一脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；再將高沸點有機物脫出：該第一吸附轉輪之高溫脫附區的一側係由一第二熱氣輸送管路來輸送由該第二加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪之高溫脫附區的另一側則透過一第一高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路內；輸送欲再吸附之氣體：該第二吸附轉輪之吸附區的一側係由該第一淨氣排放管路來輸送欲進行再吸附之氣體，而該第二吸附轉輪之吸附區的另一側則透過一第二淨氣排放管路來輸送經過再吸附後之氣體；輸入用來冷卻之氣體：該第二吸附轉輪之冷卻區的另一側係由一第二冷卻氣進氣管路來輸入用來冷卻之氣體，而該第二吸附轉輪之冷卻區的一側則透過一第二冷卻氣輸送管路來連接至該第三加熱裝置，以將經過該第二吸附轉輪之冷卻區的氣體輸送到該第三加熱裝置內； 輸送高溫熱氣進行脫附：該第二吸附轉輪之脫附區的一側係由一第三熱氣輸送管路來輸送該第三加熱裝置內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路係設有一第三熱氣旁通管路，透過該第三熱氣旁通管路連接至該第四加熱裝置，而該第二吸附轉輪之脫附區的另一側則透過一第二脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；以及再將高沸點有機物脫出：該第二吸附轉輪之高溫脫附區的一側係由一第四熱氣輸送管路來輸送由該第四加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪之高溫脫附區的另一側則透過一第二高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路內。 A runner method with high temperature desorption is provided with a first adsorption runner, a second adsorption runner, a first heating device, a second heating device, a third heating device and a fourth heating device, The main steps of the runner method include: input of gas to be adsorbed: one side of the adsorption area of the first adsorption runner is inputted by a waste gas inlet line, and the first adsorption runner The other side of the adsorption area is through a The first clean gas discharge line is used to transport the gas after adsorption; the gas used for cooling is input: the other side of the cooling area of the first adsorption runner is input by a first cooling gas inlet line for Cooled gas, and one side of the cooling zone of the first adsorption runner is connected to the first heating device through a first cooling gas delivery line to pass the gas passing through the cooling zone of the first adsorption runner Transport to the first heating device; transport high-temperature hot gas for desorption: one side of the desorption area of the first adsorption runner is transported by a first hot gas delivery line to transport the high temperature generated in the first heating device Hot gas is used for desorption, and the first hot gas conveying pipeline is provided with a first hot gas bypass pipeline, which is connected to the second heating device through the first hot gas bypass pipeline, and the first adsorption runner The other side of the desorption zone transports the desorption concentrated gas after desorption through a first desorption concentrated gas pipeline; and then removes the high-boiling organic matter: the high-temperature desorption zone of the first adsorption runner On one side, a high temperature hot gas raised to a certain temperature by the second heating device is transported by a second hot gas delivery pipeline to remove high boiling point organic compounds (VOC), and the high temperature of the first adsorption runner is removed The other side of the attached area transports the high-temperature desorption concentrated gas after desorption to the first desorption concentrated gas pipeline through a first high-temperature desorption concentrated gas pipeline; conveys the gas to be re-adsorbed: the One side of the adsorption zone of the second adsorption runner is transported by the first clean gas discharge line to the gas to be re-adsorbed, while the other side of the adsorption zone of the second adsorption runner passes through a second net The gas discharge line is used to transport the re-adsorbed gas; input gas for cooling: the other side of the cooling zone of the second adsorption runner is input by a second cooling gas inlet line for cooling Gas, and one side of the cooling zone of the second adsorption runner is connected to the third heating device through a second cooling gas delivery line to convey the gas passing through the cooling zone of the second adsorption runner to In the third heating device; Delivering high-temperature hot gas for desorption: One side of the desorption area of the second adsorption runner is a third hot-gas delivery pipeline to convey high-temperature hot gas generated in the third heating device for desorption, and the first The third hot gas conveying pipeline is provided with a third hot gas bypass pipeline, which is connected to the fourth heating device through the third hot gas bypass pipeline, and the other side of the desorption zone of the second adsorption runner passes through A second desorption concentrated gas pipeline to deliver desorbed concentrated gas after desorption; and then to remove high-boiling organic matter: one side of the high-temperature desorption zone of the second adsorption runner is a fourth hot gas The conveying pipeline conveys the high-temperature hot gas raised to a certain temperature in the fourth heating device to remove high-boiling point organic compounds (VOC), and the other side of the high-temperature desorption zone of the second adsorption runner passes through A second high-temperature desorption concentrated gas pipeline conveys the desorbed high-temperature desorption concentrated gas into the second desorption concentrated gas pipeline. 一種具高溫脫附之轉輪方法，係設有一第一吸附轉輪、一第二吸附轉輪、一第一加熱裝置、一第二加熱裝置、一第三加熱裝置及一第四加熱裝置，該轉輪方法的主要步驟係包括；輸入待吸附之氣體：該第一吸附轉輪之吸附區的一側係由一廢氣進氣管路來輸入待吸附之氣體，而該第一吸附轉輪之吸附區的另一側則透過一第一淨氣排放管路來輸送經過吸附後之氣體；輸入用來冷卻之氣體：該第一吸附轉輪之冷卻區的一側係由一第一冷卻氣進氣管路來輸入用來冷卻之氣體，而該第一吸附轉輪之冷卻區的另一側則透過一第一冷卻氣輸送管路來連接至該第一加熱裝置，以將經過該第一吸附轉輪之冷卻區的氣體輸送到該第一加熱裝置內；輸送高溫熱氣進行脫附：該第一吸附轉輪之脫附區的另一側係由一第一熱氣輸送管路來輸送該第一加熱裝置內所產生的高溫熱氣以進行脫 附，且該第一熱氣輸送管路係設有一第一熱氣旁通管路，透過該第一熱氣旁通管路連接至該第二加熱裝置，而該第一吸附轉輪之脫附區的一側則透過一第一脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；再將高沸點有機物脫出：該第一吸附轉輪之高溫脫附區的另一側係由一第二熱氣輸送管路來輸送由該第二加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪之高溫脫附區的一側則透過一第一高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路內；輸送欲再吸附之氣體：該第二吸附轉輪之吸附區的一側係由該第一淨氣排放管路來輸送欲進行再吸附之氣體，而該第二吸附轉輪之吸附區的另一側則透過一第二淨氣排放管路來輸送經過再吸附後之氣體；輸入用來冷卻之氣體：該第二吸附轉輪之冷卻區的另一側係由一第二冷卻氣進氣管路來輸入用來冷卻之氣體，而該第二吸附轉輪之冷卻區的一側則透過一第二冷卻氣輸送管路來連接至該第三加熱裝置，以將經過該第二吸附轉輪之冷卻區的氣體輸送到該第三加熱裝置內；輸送高溫熱氣進行脫附：該第二吸附轉輪之脫附區的一側係由一第三熱氣輸送管路來輸送該第三加熱裝置內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路係設有一第三熱氣旁通管路，透過該第三熱氣旁通管路連接至該第四加熱裝置，而該第二吸附轉輪之脫附區的另一側則透過一第二脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；以及再將高沸點有機物脫出：該第二吸附轉輪之高溫脫附區的一側係由一第四熱氣輸送管路來輸送由該第四加熱裝置內所提升到一定溫度的高溫 熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪之高溫脫附區的另一側則透過一第二高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路內。 A runner method with high temperature desorption is provided with a first adsorption runner, a second adsorption runner, a first heating device, a second heating device, a third heating device and a fourth heating device, The main steps of the runner method include: input of gas to be adsorbed: one side of the adsorption area of the first adsorption runner is inputted by a waste gas inlet line, and the first adsorption runner The other side of the adsorption zone transports the gas after adsorption through a first clean gas discharge line; input gas for cooling: one side of the cooling zone of the first adsorption runner is cooled by a first The gas inlet line is used to input the gas for cooling, and the other side of the cooling area of the first adsorption runner is connected to the first heating device through a first cooling gas delivery line to pass through the The gas in the cooling zone of the first adsorption runner is delivered to the first heating device; high-temperature hot gas is delivered for desorption: the other side of the desorption zone of the first adsorption runner is provided by a first hot gas delivery pipeline The high-temperature hot gas generated in the first heating device is transported to remove Attached, and the first hot gas delivery pipeline is provided with a first hot gas bypass pipeline, connected to the second heating device through the first hot gas bypass pipeline, and the desorption area of the first adsorption runner One side transports the desorbed concentrated gas through a first desorbed concentrated gas pipeline; the high-boiling organic matter is then removed: the other side of the high-temperature desorption zone of the first adsorption runner is A second hot gas conveying pipeline conveys the high-temperature hot gas raised to a certain temperature in the second heating device to remove high-boiling organic compounds (VOC), and one of the high-temperature desorption areas of the first adsorption runner The side transports the high-temperature desorption concentrated gas after desorption to the first desorption concentrated gas pipeline through a first high-temperature desorption concentrated gas pipeline; conveys the gas to be re-adsorbed: the second adsorption runner One side of the adsorption zone is transported by the first clean gas discharge line to the gas to be re-adsorbed, and the other side of the adsorption zone of the second adsorption runner is through a second clean gas discharge line Transmit the gas after re-adsorption; input the gas for cooling: the other side of the cooling area of the second adsorption runner is supplied with a gas for cooling by a second cooling gas inlet line, and the first One side of the cooling zone of the second adsorption runner is connected to the third heating device through a second cooling gas delivery line to convey the gas passing through the cooling zone of the second adsorption runner to the third heating device Inside; conveying high temperature hot gas for desorption: one side of the desorption area of the second adsorption runner is a third hot gas conveying pipeline to convey the high temperature hot gas generated in the third heating device for desorption, and The third hot gas delivery pipeline is provided with a third hot gas bypass pipeline, which is connected to the fourth heating device through the third hot gas bypass pipeline, and the other side of the desorption zone of the second adsorption runner Then, a second desorption concentrated gas pipeline is used to transport the desorbed concentrated gas after desorption; and the high-boiling organic matter is removed again: the side of the high-temperature desorption zone of the second adsorption runner is composed of a first Four hot gas conveying pipelines to convey the high temperature raised to a certain temperature by the fourth heating device Hot gas to remove high-boiling organics (VOC), and the other side of the high-temperature desorption zone of the second adsorption runner is transported through a second high-temperature desorption concentrated gas pipeline after desorption Attach concentrated gas to the second desorption concentrated gas pipeline. 一種具高溫脫附之轉輪方法，係設有一第一吸附轉輪、一第二吸附轉輪、一第一加熱裝置、一第二加熱裝置、一第三加熱裝置及一第四加熱裝置，該轉輪方法的主要步驟係包括；輸入待吸附之氣體：該第一吸附轉輪之吸附區的一側係由一廢氣進氣管路來輸入待吸附之氣體，而該第一吸附轉輪之吸附區的另一側則透過一第一淨氣排放管路來輸送經過吸附後之氣體；輸入用來冷卻之氣體：該第一吸附轉輪之冷卻區的另一側係由一第一冷卻氣進氣管路來輸入用來冷卻之氣體，而該第一吸附轉輪之冷卻區的一側則透過一第一冷卻氣輸送管路來連接至該第一加熱裝置，以將經過該第一吸附轉輪之冷卻區的氣體輸送到該第一加熱裝置內；輸送高溫熱氣進行脫附：該第一吸附轉輪之脫附區的一側係由一第一熱氣輸送管路來輸送該第一加熱裝置內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路係設有一第一熱氣旁通管路，透過該第一熱氣旁通管路連接至該第二加熱裝置，而該第一吸附轉輪之脫附區的另一側則透過一第一脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；再將高沸點有機物脫出：該第一吸附轉輪之高溫脫附區的一側係由一第二熱氣輸送管路來輸送由該第二加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第一吸附轉輪之高溫脫附區 的另一側則透過一第一高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第一脫附濃縮氣體管路內；輸送欲再吸附之氣體：該第二吸附轉輪之吸附區的一側係由該第一淨氣排放管路來輸送欲進行再吸附之氣體，而該第二吸附轉輪之吸附區的另一側則透過一第二淨氣排放管路來輸送經過再吸附後之氣體；輸入用來冷卻之氣體：該第二吸附轉輪之冷卻區的一側係由一第二冷卻氣進氣管路來輸入用來冷卻之氣體，而該第二吸附轉輪之冷卻區的另一側則透過一第二冷卻氣輸送管路來連接至該第三加熱裝置，以將經過該第二吸附轉輪之冷卻區的氣體輸送到該第三加熱裝置內；輸送高溫熱氣進行脫附：該第二吸附轉輪之脫附區的另一側係由一第三熱氣輸送管路來輸送該第三加熱裝置內所產生的高溫熱氣以進行脫附，且該第三熱氣輸送管路係設有一第三熱氣旁通管路，透過該第三熱氣旁通管路連接至該第四加熱裝置，而該第二吸附轉輪之脫附區的一側則透過一第二脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；以及再將高沸點有機物脫出：該第二吸附轉輪之高溫脫附區的另一側係由一第四熱氣輸送管路來輸送由該第四加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該第二吸附轉輪之高溫脫附區的一側則透過一第二高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該第二脫附濃縮氣體管路內。 A runner method with high temperature desorption is provided with a first adsorption runner, a second adsorption runner, a first heating device, a second heating device, a third heating device and a fourth heating device, The main steps of the runner method include: input of gas to be adsorbed: one side of the adsorption area of the first adsorption runner is inputted by a waste gas inlet line, and the first adsorption runner The other side of the adsorption zone transports the gas after adsorption through a first clean gas discharge line; input gas for cooling: the other side of the cooling zone of the first adsorption runner is composed of a first The cooling gas inlet line is used to input the gas used for cooling, and the side of the cooling area of the first adsorption runner is connected to the first heating device through a first cooling gas delivery line to pass through the The gas in the cooling zone of the first adsorption runner is delivered to the first heating device; high-temperature hot gas is delivered for desorption: one side of the desorption zone of the first adsorption runner is conveyed by a first hot gas delivery pipeline The high-temperature hot gas generated in the first heating device is used for desorption, and the first hot gas delivery pipeline is provided with a first hot gas bypass pipeline, which is connected to the second heating through the first hot gas bypass pipeline Device, and the other side of the desorption zone of the first adsorption runner is to transport the desorbed concentrated gas after desorption through a first desorbed concentrated gas pipeline; then remove the high-boiling organic matter: the first One side of the high-temperature desorption zone of an adsorption runner is transported by a second hot gas conveying pipeline to the high-temperature hot gas raised to a certain temperature in the second heating device to remove high-boiling organics (VOC), And the high temperature desorption zone of the first adsorption runner On the other side, the high-temperature desorption concentrated gas after desorption is transferred to the first desorption concentrated gas line through a first high-temperature desorption concentrated gas line; the gas to be re-adsorbed: the second One side of the adsorption zone of the adsorption rotor is transported by the first clean gas discharge line to be re-adsorbed, and the other side of the adsorption zone of the second adsorption runner is discharged through a second clean gas Pipeline to transport the re-adsorbed gas; enter the gas for cooling: one side of the cooling area of the second adsorption runner is a second cooling gas inlet line to input the gas for cooling, and The other side of the cooling zone of the second adsorption runner is connected to the third heating device through a second cooling gas delivery line to convey the gas passing through the cooling zone of the second adsorption runner to the first Three heating devices; transport high-temperature hot gas for desorption: the other side of the desorption zone of the second adsorption runner is transported by a third hot gas delivery pipeline to transport high-temperature hot gas generated in the third heating device Desorption, and the third hot gas delivery pipeline is provided with a third hot gas bypass pipeline, connected to the fourth heating device through the third hot gas bypass pipeline, and the desorption zone of the second adsorption runner One side is transported through a second desorption concentrated gas pipeline to pass through the desorption concentrated gas after desorption; and then the high-boiling organic matter is removed: the other side of the high-temperature desorption zone of the second adsorption runner A fourth hot gas delivery pipeline is used to deliver high temperature hot gas raised to a certain temperature in the fourth heating device to remove high boiling point organic compounds (VOC), and the high temperature desorption zone of the second adsorption runner One side of the pump transports the high-temperature desorption concentrated gas after desorption into the second desorption concentrated gas pipeline through a second high-temperature desorption concentrated gas pipeline. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第一脫附濃縮氣體管路的另一端及該第二脫附濃縮氣體管路的另 一端係進一步與一焚燒裝置連接。 The runner method with high temperature desorption as described in item 1, 2, 3 or 4 of the patent application scope, wherein the other end of the first desorption concentrated gas pipeline and the other of the second desorption concentrated gas pipeline One end is further connected to an incinerator. 如申請專利範圍第5項所述之具高溫脫附之轉輪方法，其中該焚燒裝置係進一步為直燃式焚燒爐(TO)、觸媒爐或蓄熱式焚燒爐(RTO)之其中任一。 The runner method with high temperature desorption as described in item 5 of the patent application scope, wherein the incinerator is any one of a direct combustion incinerator (TO), a catalyst furnace or a regenerative incinerator (RTO) . 如申請專利範圍第6項所述之具高溫脫附之轉輪方法，其中該蓄熱式焚燒爐(RTO)係設有入口及出口，該入口係與該第一脫附濃縮氣體管路及該第二脫附濃縮氣體管路連接，該出口則連接至一煙囪。 The runner method with high temperature desorption as described in item 6 of the patent application scope, wherein the regenerative incinerator (RTO) is provided with an inlet and an outlet, the inlet is connected with the first desorption concentrated gas pipeline and the The second desorption concentrated gas pipeline is connected, and the outlet is connected to a chimney. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第二淨氣排放管路的另一端係與一煙囪連接。 The runner method with high temperature desorption as described in item 1, 2, 3 or 4 of the patent application scope, wherein the other end of the second clean gas discharge pipe is connected to a chimney. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第一加熱裝置、第二加熱裝置、第三加熱裝置及第四加熱裝置係進一步為加熱器、管道加熱器或熱交換器之其中任一，該加熱器係採用電熱絲、電熱管或電熱片之其中任一，該管道加熱器係採用氣體燃料或液體燃料之其中任一。 The runner method with high temperature desorption as described in item 1, 2, 3 or 4 of the patent application scope, wherein the first heating device, the second heating device, the third heating device and the fourth heating device are further heated Any one of the heater, pipe heater or heat exchanger, the heater is any one of electric heating wire, electric heating tube or electric heating plate, the pipe heater is any one of gas fuel or liquid fuel. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第一熱氣旁通管路係進一步設有一第一熱氣旁通控制閥門，以控制該熱氣旁通管路的風量。 The runner method with high temperature desorption as described in item 1, 2, 3 or 4 of the patent application scope, wherein the first hot gas bypass line is further provided with a first hot gas bypass control valve to control the hot gas The air volume of the bypass line. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第三熱氣旁通管路係進一步設有一第三熱氣旁通控制閥門，以控制該熱氣旁通管路的風量。 The runner method with high temperature desorption as described in item 1, 2, 3 or 4 of the patent application scope, wherein the third hot gas bypass line is further provided with a third hot gas bypass control valve to control the hot gas The air volume of the bypass line. 如申請專利範圍第1或3項所述之具高溫脫附之轉輪方法，其中該廢氣進氣管路係進一步設有一廢氣連通管路，該廢氣連通管路係與該第 一冷卻氣進氣管路連接，該廢氣連通管路係進一步設有一廢氣連通控制閥門，以控制該廢氣連通管路的風量。 The runner method with high temperature desorption as described in item 1 or 3 of the patent application scope, wherein the exhaust gas intake line is further provided with an exhaust gas communication line, the exhaust gas communication line is connected to the A cooling gas inlet pipeline is connected, and the exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. 如申請專利範圍第1項所述之具高溫脫附之轉輪方法，其中該第一淨氣排放管路係進一步設有一第一淨氣連通管路，該第一淨氣連通管路係與該第二冷卻氣進氣管路連接，該第一淨氣連通管路係進一步設有一第一淨氣連通控制閥門，以控制該第一淨氣連通管路的風量。 The runner method with high temperature desorption as described in item 1 of the patent application scope, wherein the first clean gas discharge pipeline is further provided with a first clean gas communication pipeline, the first clean gas communication pipeline is The second cooling air intake line is connected, and the first clean air communication line is further provided with a first clean air communication control valve to control the air volume of the first clean air communication line. 如申請專利範圍第2項所述之具高溫脫附之轉輪方法，其中該第一淨氣排放管路係進一步設有一第一淨氣連通管路，該第一淨氣連通管路係與該第一冷卻氣進氣管路連接，該第一淨氣連通管路係進一步設有一第一淨氣連通控制閥門，以控制該第一淨氣連通管路的風量。 The runner method with high temperature desorption as described in item 2 of the patent application scope, wherein the first clean gas discharge pipeline is further provided with a first clean gas communication pipeline, the first clean gas communication pipeline is The first cooling air intake line is connected, and the first clean air communication line is further provided with a first clean air communication control valve to control the air volume of the first clean air communication line. 如申請專利範圍第2或3項所述之具高溫脫附之轉輪方法，其中該第二淨氣排放管路係進一步設有一第二淨氣連通管路，該第二淨氣連通管路係與該第二冷卻氣進氣管路連接，該第二淨氣連通管路係進一步設有一第二淨氣連通控制閥門，以控制該第二淨氣連通管路的風量。 The runner method with high temperature desorption as described in item 2 or 3 of the patent application scope, wherein the second clean air discharge pipeline is further provided with a second clean air communication pipeline, the second clean air communication pipeline It is connected to the second cooling gas intake line. The second clean gas communication line is further provided with a second clean gas communication control valve to control the air volume of the second clean gas communication line. 如申請專利範圍第4項所述之具高溫脫附之轉輪方法，其中該第一淨氣排放管路係進一步設有一第一淨氣第一連通管路，該第一淨氣第一連通管路係與該第一冷卻氣進氣管路連接，該第一淨氣第一連通管路係進一步設有一第一淨氣第一連通控制閥門，以控制該第一淨氣第一連通管路的風量。 The runner method with high temperature desorption as described in item 4 of the patent application scope, wherein the first clean gas discharge line is further provided with a first clean gas first communication line, the first clean gas is first The communication pipeline is connected to the first cooling gas intake pipeline, and the first clean gas first communication pipeline is further provided with a first clean gas first communication control valve to control the first clean gas The air volume of the first communication line. 如申請專利範圍第4項所述之具高溫脫附之轉輪方法，其中該第一淨氣排放管路係進一步設有一第一淨氣第二連通管路，該第一淨氣第二連通管路係與該第二冷卻氣進氣管路連接，該第一淨氣第二連通管路係 進一步設有一第一淨氣第二連通控制閥門，以控制該第一淨氣第二連通管路的風量。 The runner method with high temperature desorption as described in item 4 of the patent application scope, wherein the first clean gas discharge pipeline is further provided with a first clean gas second communication pipeline, and the first clean gas second communication The pipeline system is connected to the second cooling gas intake pipeline, and the first clean gas second communication pipeline system A first clean gas second communication control valve is further provided to control the air volume of the first clean gas second communication pipeline. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第一脫附濃縮氣體管路係進一步設有一風機。 The runner method with high temperature desorption as described in item 1, 2, 3 or 4 of the patent application scope, wherein the first desorption concentrated gas pipeline is further provided with a fan. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第二脫附濃縮氣體管路係進一步設有一風機。 The runner method with high temperature desorption as described in item 1, 2, 3 or 4 of the patent application scope, wherein the second desorption concentrated gas pipeline is further provided with a fan. 如申請專利範圍第1、2、3或4項所述之具高溫脫附之轉輪方法，其中該第二淨氣排放管路係進一步設有一風機。 The runner method with high temperature desorption as described in item 1, 2, 3, or 4 of the patent application scope, wherein the second clean gas discharge pipeline is further provided with a fan. 一種具高溫脫附之轉輪系統，係包括：一第一吸附轉輪，該第一吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該一廢氣進氣管路的一端係連接至該第一吸附轉輪之吸附區的一側，該一第一淨氣排放管路的一端係與該第一吸附轉輪之吸附區的另一側連接，該一第一冷卻氣進氣管路的一端係與該第一吸附轉輪之冷卻區之一側連接，該一第一冷卻氣輸送管路的一端係與該第一吸附轉輪之冷卻區的另一側連接，該一第一熱氣輸送管路的一端係與該第一吸附轉輪之脫附區的另一側連接，該一第二熱氣輸送管路的一端係與該第一吸附轉輪之高溫脫附區的另一側連接，該一第一脫附濃縮氣體管路的一端係與該第一吸附轉輪之脫附區的一側連接，該一第一高溫脫附濃縮氣體管路的一端係與該第一吸附轉輪之高溫脫附區的一側連接，該第一高溫脫附濃縮氣體管路的另一端係與該第一脫附濃縮氣體管路連接；一第二吸附轉輪，該第二吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該第一淨氣排放管路的一端係連接至該第二吸附轉輪之吸附 區的一側，該一第二淨氣排放管路的一端係與該第二吸附轉輪之吸附區的另一側連接，該一第二冷卻氣進氣管路的一端係與該第二吸附轉輪之冷卻區之一側連接，該一第二冷卻氣輸送管路的一端係與該第二吸附轉輪之冷卻區的另一側連接，該一第三熱氣輸送管路的一端係與該第二吸附轉輪之脫附區的另一側連接，該一第四熱氣輸送管路的一端係與該第二吸附轉輪之高溫脫附區的另一側連接，該一第二脫附濃縮氣體管路的一端係與該第二吸附轉輪之脫附區的一側連接，該一第二高溫脫附濃縮氣體管路的一端係與該第二吸附轉輪之高溫脫附區的一側連接，該第二高溫脫附濃縮氣體管路的另一端係與該第二脫附濃縮氣體管路連接；一第一加熱裝置，該第一冷卻氣輸送管路的另一端係與該第一加熱裝置連接，該第一熱氣輸送管路的另一端係與該第一加熱裝置連接；一第二加熱裝置，該第一熱氣輸送管路係設有一第一熱氣旁通管路，該第一熱氣旁通管路的另一端係與該第二加熱裝置連接，該第二熱氣輸送管路的另一端係與該第二加熱裝置連接；一第三加熱裝置，該第二冷卻氣輸送管路的另一端係與該第三加熱裝置連接，該第三熱氣輸送管路的另一端係與該第三加熱裝置連接；以及一第四加熱裝置，該第三熱氣輸送管路係設有一第三熱氣旁通管路，該第三熱氣旁通管路的另一端係與該第四加熱裝置連接，該第四熱氣輸送管路的另一端係與該第四加熱裝置連接。 A runner system with high temperature desorption includes: a first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone, a desorption zone and a high temperature desorption zone, the exhaust gas inlet pipe One end of the path is connected to one side of the adsorption zone of the first adsorption runner, and one end of the first clean gas discharge line is connected to the other side of the adsorption zone of the first adsorption runner. One end of a cooling gas inlet pipe is connected to one side of the cooling zone of the first adsorption runner, and one end of the first cooling gas delivery pipe is connected to the other of the cooling zone of the first adsorption runner Side, one end of the first hot gas delivery line is connected to the other side of the desorption zone of the first adsorption runner, and one end of the second hot gas delivery line is connected to the first adsorption runner The other side of the high temperature desorption zone is connected, one end of the first desorption concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption runner, the first high temperature desorption concentrated gas pipeline One end is connected to one side of the high temperature desorption zone of the first adsorption runner, the other end of the first high temperature desorption concentrated gas pipeline is connected to the first desorption concentrated gas pipeline; a second adsorption The runner, the second adsorption runner is provided with an adsorption zone, a cooling zone, a desorption zone, and a high-temperature desorption zone, and one end of the first clean gas discharge pipe is connected to the adsorption of the second adsorption runner On one side of the zone, one end of the second clean gas discharge line is connected to the other side of the adsorption zone of the second adsorption runner, and one end of the second cooling gas intake line is connected with the second One side of the cooling zone of the adsorption rotor is connected, one end of the second cooling gas delivery pipeline is connected to the other side of the cooling zone of the second adsorption rotor, and one end of the third hot gas delivery pipeline is It is connected to the other side of the desorption zone of the second adsorption runner, and one end of the fourth hot gas delivery pipeline is connected to the other side of the high-temperature desorption zone of the second adsorption runner. One end of the desorption concentrated gas pipeline is connected to one side of the desorption area of the second adsorption runner, and one end of the second high-temperature desorption concentrated gas pipeline is connected to the high-temperature desorption of the second adsorption runner Connected to one side of the zone, the other end of the second high temperature desorption concentrated gas pipeline is connected to the second desorption concentrated gas pipeline; a first heating device, the other end of the first cooling gas delivery pipeline is Connected to the first heating device, the other end of the first hot gas delivery line is connected to the first heating device; a second heating device, the first hot gas delivery line is provided with a first hot gas bypass line , The other end of the first hot gas bypass line is connected to the second heating device, the other end of the second hot gas delivery line is connected to the second heating device; a third heating device, the second cooling The other end of the gas delivery line is connected to the third heating device, the other end of the third hot gas delivery line is connected to the third heating device; and a fourth heating device, the third hot gas delivery line is A third hot gas bypass line is provided, the other end of the third hot gas bypass line is connected to the fourth heating device, and the other end of the fourth hot gas delivery line is connected to the fourth heating device. 一種具高溫脫附之轉輪系統，係包括：一第一吸附轉輪，該第一吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該一廢氣進氣管路的一端係連接至該第一吸附轉輪之吸附區 的一側，該一第一淨氣排放管路的一端係與該第一吸附轉輪之吸附區的另一側連接，該一第一冷卻氣進氣管路的一端係與該第一吸附轉輪之冷卻區之另一側連接，該一第一冷卻氣輸送管路的一端係與該第一吸附轉輪之冷卻區的一側連接，該一第一熱氣輸送管路的一端係與該第一吸附轉輪之脫附區的一側連接，該一第二熱氣輸送管路的一端係與該第一吸附轉輪之高溫脫附區的一側連接，該一第一脫附濃縮氣體管路的一端係與該第一吸附轉輪之脫附區的另一側連接，該一第一高溫脫附濃縮氣體管路的一端係與該第一吸附轉輪之高溫脫附區的另一側連接，該第一高溫脫附濃縮氣體管路的另一端係與該第一脫附濃縮氣體管路連接；一第二吸附轉輪，該第二吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該第一淨氣排放管路的一端係連接至該第二吸附轉輪之吸附區的一側，該一第二淨氣排放管路的一端係與該第二吸附轉輪之吸附區的另一側連接，該一第二冷卻氣進氣管路的一端係與該第二吸附轉輪之冷卻區之另一側連接，該一第二冷卻氣輸送管路的一端係與該第二吸附轉輪之冷卻區的一側連接，該一第三熱氣輸送管路的一端係與該第二吸附轉輪之脫附區的一側連接，該一第四熱氣輸送管路的一端係與該第二吸附轉輪之高溫脫附區的一側連接，該一第二脫附濃縮氣體管路的一端係與該第二吸附轉輪之脫附區的另一側連接，該一第二高溫脫附濃縮氣體管路的一端係與該第二吸附轉輪之高溫脫附區的另一側連接，該第二高溫脫附濃縮氣體管路的另一端係與該第二脫附濃縮氣體管路連接；一第一加熱裝置，該第一冷卻氣輸送管路的另一端係與該第一加熱裝置連接，該第一熱氣輸送管路的另一端係與該第一加熱裝置連接； 一第二加熱裝置，該第一熱氣輸送管路係設有一第一熱氣旁通管路，該第一熱氣旁通管路的另一端係與該第二加熱裝置連接，該第二熱氣輸送管路的另一端係與該第二加熱裝置連接；一第三加熱裝置，該第二冷卻氣輸送管路的另一端係與該第三加熱裝置連接，該第三熱氣輸送管路的另一端係與該第三加熱裝置連接；以及一第四加熱裝置，該第三熱氣輸送管路係設有一第三熱氣旁通管路，該第三熱氣旁通管路的另一端係與該第四加熱裝置連接，該第四熱氣輸送管路的另一端係與該第四加熱裝置連接。 A runner system with high temperature desorption includes: a first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone, a desorption zone and a high temperature desorption zone, the exhaust gas inlet pipe One end of the road is connected to the adsorption area of the first adsorption rotor On one side, one end of the first clean gas discharge line is connected to the other side of the adsorption area of the first adsorption runner, and one end of the first cooling gas intake line is connected with the first adsorption The other side of the cooling zone of the runner is connected, one end of the first cooling gas delivery line is connected to one side of the cooling zone of the first adsorption runner, and one end of the first hot gas delivery line is connected to One side of the desorption zone of the first adsorption runner is connected, and one end of the second hot gas delivery pipeline is connected to one side of the high-temperature desorption zone of the first adsorption runner, the first desorption concentration One end of the gas pipeline is connected to the other side of the desorption zone of the first adsorption runner, and one end of the first high-temperature desorption concentrated gas pipeline is connected to the high-temperature desorption zone of the first adsorption runner The other side is connected, and the other end of the first high-temperature desorption concentrated gas pipeline is connected to the first desorption concentrated gas pipeline; a second adsorption runner, the second adsorption runner is provided with an adsorption area, In the cooling zone, the desorption zone and the high-temperature desorption zone, one end of the first clean gas discharge pipe is connected to one side of the adsorption zone of the second adsorption runner, and one end of the second clean gas discharge pipe is It is connected to the other side of the adsorption zone of the second adsorption runner, and one end of the second cooling gas inlet line is connected to the other side of the cooling zone of the second adsorption runner, the second cooling One end of the gas conveying pipeline is connected to one side of the cooling zone of the second adsorption runner, and one end of the third hot gas conveying pipeline is connected to one side of the desorption zone of the second adsorption runner. One end of a fourth hot gas delivery pipeline is connected to one side of the high-temperature desorption zone of the second adsorption runner, and one end of the second desorption concentrated gas pipeline is desorbed from the second adsorption runner The other side of the zone is connected, and one end of the second high-temperature desorption concentrated gas pipeline is connected to the other side of the high-temperature desorption zone of the second adsorption runner. The other end is connected to the second desorbed concentrated gas line; a first heating device, the other end of the first cooling gas delivery line is connected to the first heating device, the other of the first hot gas delivery line One end is connected to the first heating device; A second heating device, the first hot gas delivery line is provided with a first hot gas bypass line, the other end of the first hot gas bypass line is connected to the second heating device, and the second hot gas delivery tube The other end of the circuit is connected to the second heating device; a third heating device, the other end of the second cooling gas delivery line is connected to the third heating device, and the other end of the third hot gas delivery line is Connected to the third heating device; and a fourth heating device, the third hot gas delivery line is provided with a third hot gas bypass line, the other end of the third hot gas bypass line is connected to the fourth heating The device is connected, and the other end of the fourth hot gas delivery pipeline is connected to the fourth heating device. 一種具高溫脫附之轉輪系統，係包括：一第一吸附轉輪，該第一吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該一廢氣進氣管路的一端係連接至該第一吸附轉輪之吸附區的一側，該一第一淨氣排放管路的一端係與該第一吸附轉輪之吸附區的另一側連接，該一第一冷卻氣進氣管路的一端係與該第一吸附轉輪之冷卻區之一側連接，該一第一冷卻氣輸送管路的一端係與該第一吸附轉輪之冷卻區的另一側連接，該一第一熱氣輸送管路的一端係與該第一吸附轉輪之脫附區的另一側連接，該一第二熱氣輸送管路的一端係與該第一吸附轉輪之高溫脫附區的另一側連接，該一第一脫附濃縮氣體管路的一端係與該第一吸附轉輪之脫附區的一側連接，該一第一高溫脫附濃縮氣體管路的一端係與該第一吸附轉輪之高溫脫附區的一側連接，該第一高溫脫附濃縮氣體管路的另一端係與該第一脫附濃縮氣體管路連接；一第二吸附轉輪，該第二吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該第一淨氣排放管路的一端係連接至該第二吸附轉輪之吸附 區的一側，該一第二淨氣排放管路的一端係與該第二吸附轉輪之吸附區的另一側連接，該一第二冷卻氣進氣管路的一端係與該第二吸附轉輪之冷卻區之另一側連接，該一第二冷卻氣輸送管路的一端係與該第二吸附轉輪之冷卻區的一側連接，該一第三熱氣輸送管路的一端係與該第二吸附轉輪之脫附區的一側連接，該一第四熱氣輸送管路的一端係與該第二吸附轉輪之高溫脫附區的一側連接，該一第二脫附濃縮氣體管路的一端係與該第二吸附轉輪之脫附區的另一側連接，該一第二高溫脫附濃縮氣體管路的一端係與該第二吸附轉輪之高溫脫附區的另一側連接，該第二高溫脫附濃縮氣體管路的另一端係與該第二脫附濃縮氣體管路連接；一第一加熱裝置，該第一冷卻氣輸送管路的另一端係與該第一加熱裝置連接，該第一熱氣輸送管路的另一端係與該第一加熱裝置連接；一第二加熱裝置，該第一熱氣輸送管路係設有一第一熱氣旁通管路，該第一熱氣旁通管路的另一端係與該第二加熱裝置連接，該第二熱氣輸送管路的另一端係與該第二加熱裝置連接；一第三加熱裝置，該第二冷卻氣輸送管路的另一端係與該第三加熱裝置連接，該第三熱氣輸送管路的另一端係與該第三加熱裝置連接；以及一第四加熱裝置，該第三熱氣輸送管路係設有一第三熱氣旁通管路，該第三熱氣旁通管路的另一端係與該第四加熱裝置連接，該第四熱氣輸送管路的另一端係與該第四加熱裝置連接。 A runner system with high temperature desorption includes: a first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone, a desorption zone and a high temperature desorption zone, the exhaust gas inlet pipe One end of the path is connected to one side of the adsorption zone of the first adsorption runner, and one end of the first clean gas discharge line is connected to the other side of the adsorption zone of the first adsorption runner. One end of a cooling gas inlet pipe is connected to one side of the cooling zone of the first adsorption runner, and one end of the first cooling gas delivery pipe is connected to the other of the cooling zone of the first adsorption runner Side, one end of the first hot gas delivery line is connected to the other side of the desorption zone of the first adsorption runner, and one end of the second hot gas delivery line is connected to the first adsorption runner The other side of the high temperature desorption zone is connected, one end of the first desorption concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption runner, the first high temperature desorption concentrated gas pipeline One end is connected to one side of the high temperature desorption zone of the first adsorption runner, the other end of the first high temperature desorption concentrated gas pipeline is connected to the first desorption concentrated gas pipeline; a second adsorption The runner, the second adsorption runner is provided with an adsorption zone, a cooling zone, a desorption zone, and a high-temperature desorption zone, and one end of the first clean gas discharge pipe is connected to the adsorption of the second adsorption runner On one side of the zone, one end of the second clean gas discharge line is connected to the other side of the adsorption zone of the second adsorption runner, and one end of the second cooling gas intake line is connected with the second The other side of the cooling zone of the adsorption rotor is connected, one end of the second cooling gas delivery pipeline is connected to one side of the cooling zone of the second adsorption rotor, and one end of the third hot gas delivery pipeline is It is connected to one side of the desorption zone of the second adsorption runner, and one end of the fourth hot gas delivery pipe is connected to one side of the high-temperature desorption zone of the second adsorption runner, the second desorption One end of the concentrated gas pipeline is connected to the other side of the desorption zone of the second adsorption runner, and one end of the second high temperature desorption concentrated gas pipeline is connected to the high temperature desorption zone of the second adsorption runner The other end of the second high-temperature desorption concentrated gas pipeline is connected to the second desorption concentrated gas pipeline; a first heating device, the other end of the first cooling gas delivery pipeline is connected Connected to the first heating device, the other end of the first hot gas delivery line is connected to the first heating device; a second heating device, the first hot gas delivery line is provided with a first hot gas bypass line , The other end of the first hot gas bypass line is connected to the second heating device, the other end of the second hot gas delivery line is connected to the second heating device; a third heating device, the second cooling The other end of the gas delivery line is connected to the third heating device, the other end of the third hot gas delivery line is connected to the third heating device; and a fourth heating device, the third hot gas delivery line is A third hot gas bypass line is provided, the other end of the third hot gas bypass line is connected to the fourth heating device, and the other end of the fourth hot gas delivery line is connected to the fourth heating device. 一種具高溫脫附之轉輪系統，係包括：一第一吸附轉輪，該第一吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該一廢氣進氣管路的一端係連接至該第一吸附轉輪之吸附區 的一側，該一第一淨氣排放管路的一端係與該第一吸附轉輪之吸附區的另一側連接，該一第一冷卻氣進氣管路的一端係與該第一吸附轉輪之冷卻區之另一側連接，該一第一冷卻氣輸送管路的一端係與該第一吸附轉輪之冷卻區的一側連接，該一第一熱氣輸送管路的一端係與該第一吸附轉輪之脫附區的一側連接，該一第二熱氣輸送管路的一端係與該第一吸附轉輪之高溫脫附區的一側連接，該一第一脫附濃縮氣體管路的一端係與該第一吸附轉輪之脫附區的另一側連接，該一第一高溫脫附濃縮氣體管路的一端係與該第一吸附轉輪之高溫脫附區的另一側連接，該第一高溫脫附濃縮氣體管路的另一端係與該第一脫附濃縮氣體管路連接；一第二吸附轉輪，該第二吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該第一淨氣排放管路的一端係連接至該第二吸附轉輪之吸附區的一側，該一第二淨氣排放管路的一端係與該第二吸附轉輪之吸附區的另一側連接，該一第二冷卻氣進氣管路的一端係與該第二吸附轉輪之冷卻區之一側連接，該一第二冷卻氣輸送管路的一端係與該第二吸附轉輪之冷卻區的另一側連接，該一第三熱氣輸送管路的一端係與該第二吸附轉輪之脫附區的另一側連接，該一第四熱氣輸送管路的一端係與該第二吸附轉輪之高溫脫附區的另一側連接，該一第二脫附濃縮氣體管路的一端係與該第二吸附轉輪之脫附區的一側連接，該一第二高溫脫附濃縮氣體管路的一端係與該第二吸附轉輪之高溫脫附區的一側連接，該第二高溫脫附濃縮氣體管路的另一端係與該第二脫附濃縮氣體管路連接；一第一加熱裝置，該第一冷卻氣輸送管路的另一端係與該第一加熱裝置連接，該第一熱氣輸送管路的另一端係與該第一加熱裝置連接； 一第二加熱裝置，該第一熱氣輸送管路係設有一第一熱氣旁通管路，該第一熱氣旁通管路的另一端係與該第二加熱裝置連接，該第二熱氣輸送管路的另一端係與該第二加熱裝置連接；一第三加熱裝置，該第二冷卻氣輸送管路的另一端係與該第三加熱裝置連接，該第三熱氣輸送管路的另一端係與該第三加熱裝置連接；以及一第四加熱裝置，該第三熱氣輸送管路係設有一第三熱氣旁通管路，該第三熱氣旁通管路的另一端係與該第四加熱裝置連接，該第四熱氣輸送管路的另一端係與該第四加熱裝置連接。 A runner system with high temperature desorption includes: a first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone, a desorption zone and a high temperature desorption zone, the exhaust gas inlet pipe One end of the road is connected to the adsorption area of the first adsorption rotor On one side, one end of the first clean gas discharge line is connected to the other side of the adsorption area of the first adsorption runner, and one end of the first cooling gas intake line is connected with the first adsorption The other side of the cooling zone of the runner is connected, one end of the first cooling gas delivery line is connected to one side of the cooling zone of the first adsorption runner, and one end of the first hot gas delivery line is connected to One side of the desorption zone of the first adsorption runner is connected, and one end of the second hot gas delivery pipeline is connected to one side of the high-temperature desorption zone of the first adsorption runner, the first desorption concentration One end of the gas pipeline is connected to the other side of the desorption zone of the first adsorption runner, and one end of the first high-temperature desorption concentrated gas pipeline is connected to the high-temperature desorption zone of the first adsorption runner The other side is connected, and the other end of the first high-temperature desorption concentrated gas pipeline is connected to the first desorption concentrated gas pipeline; a second adsorption runner, the second adsorption runner is provided with an adsorption area, In the cooling zone, the desorption zone and the high-temperature desorption zone, one end of the first clean gas discharge pipe is connected to one side of the adsorption zone of the second adsorption runner, and one end of the second clean gas discharge pipe is It is connected to the other side of the adsorption zone of the second adsorption runner, and one end of the second cooling gas inlet line is connected to one side of the cooling zone of the second adsorption runner, the second cooling gas One end of the conveying pipeline is connected to the other side of the cooling zone of the second adsorption runner, and one end of the third hot gas conveying pipeline is connected to the other side of the desorption zone of the second adsorption runner, One end of the fourth hot gas delivery pipeline is connected to the other side of the high-temperature desorption zone of the second adsorption runner, and one end of the second desorption concentrated gas pipeline is connected to the second adsorption runner One side of the desorption zone is connected, and one end of the second high-temperature desorption concentrated gas pipeline is connected to one side of the high-temperature desorption zone of the second adsorption runner. The other end is connected to the second desorbed concentrated gas line; a first heating device, the other end of the first cooling gas delivery line is connected to the first heating device, the other of the first hot gas delivery line One end is connected to the first heating device; A second heating device, the first hot gas delivery line is provided with a first hot gas bypass line, the other end of the first hot gas bypass line is connected to the second heating device, and the second hot gas delivery tube The other end of the circuit is connected to the second heating device; a third heating device, the other end of the second cooling gas delivery line is connected to the third heating device, and the other end of the third hot gas delivery line is Connected to the third heating device; and a fourth heating device, the third hot gas delivery line is provided with a third hot gas bypass line, the other end of the third hot gas bypass line is connected to the fourth heating The device is connected, and the other end of the fourth hot gas delivery pipeline is connected to the fourth heating device. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第一脫附濃縮氣體管路的另一端及該第二脫附濃縮氣體管路的另一端係進一步與一焚燒裝置連接。 The runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, wherein the other end of the first desorption concentrated gas line and the other of the second desorption concentrated gas line One end is further connected to an incineration device. 如申請專利範圍第25項所述之具高溫脫附之轉輪系統，其中該焚燒裝置係進一步為直燃式焚燒爐(TO)、觸媒爐或蓄熱式焚燒爐(RTO)之其中任一。 The runner system with high temperature desorption as described in item 25 of the patent scope, wherein the incinerator is any one of a direct combustion incinerator (TO), a catalyst furnace or a regenerative incinerator (RTO) . 如申請專利範圍第26項所述之具高溫脫附之轉輪系統，其中該蓄熱式焚燒爐(RTO)係設有入口及出口，該入口係與該第一脫附濃縮氣體管路及該第二脫附濃縮氣體管路連接，該出口則連接至一煙囪。 The runner system with high temperature desorption as described in item 26 of the patent application scope, wherein the regenerative incinerator (RTO) is provided with an inlet and an outlet, the inlet is connected with the first desorption concentrated gas pipeline and the The second desorption concentrated gas pipeline is connected, and the outlet is connected to a chimney. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第二淨氣排放管路的另一端係與一煙囪連接。 The runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, wherein the other end of the second clean gas discharge pipe is connected to a chimney. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第一加熱裝置、第二加熱裝置、第三加熱裝置及第四加熱裝置係進一步為加熱器、管道加熱器或熱交換器之其中任一，該加 熱器係採用電熱絲、電熱管或電熱片之其中任一，該管道加熱器係採用氣體燃料或液體燃料之其中任一。 The runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, wherein the first heating device, second heating device, third heating device and fourth heating device are further heated Heater, pipe heater or heat exchanger, the The heater adopts any one of electric heating wire, electric heating tube or electric heating sheet, and the pipeline heater adopts any one of gas fuel or liquid fuel. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第一熱氣旁通管路係進一步設有一第一熱氣旁通控制閥門，以控制該熱氣旁通管路的風量。 The runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, wherein the first hot gas bypass line is further provided with a first hot gas bypass control valve to control the hot gas The air volume of the bypass line. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第三熱氣旁通管路係進一步設有一第三熱氣旁通控制閥門，以控制該熱氣旁通管路的風量。 The runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, wherein the third hot gas bypass line is further provided with a third hot gas bypass control valve to control the hot gas The air volume of the bypass line. 如申請專利範圍第21或23項所述之具高溫脫附之轉輪系統，其中該廢氣進氣管路係進一步設有一廢氣連通管路，該廢氣連通管路係與該第一冷卻氣進氣管路連接，該廢氣連通管路係進一步設有一廢氣連通控制閥門，以控制該廢氣連通管路的風量。 The runner system with high temperature desorption as described in item 21 or 23 of the patent application scope, wherein the exhaust gas intake line is further provided with an exhaust gas communication line, the exhaust gas communication line is connected to the first cooling gas The gas pipeline is connected, and the exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. 如申請專利範圍第21項所述之具高溫脫附之轉輪系統，其中該第一淨氣排放管路係進一步設有一第一淨氣連通管路，該第一淨氣連通管路係與該第二冷卻氣進氣管路連接，該第一淨氣連通管路係進一步設有一第一淨氣連通控制閥門，以控制該第一淨氣連通管路的風量。 The runner system with high temperature desorption as described in item 21 of the patent application scope, wherein the first clean air discharge pipeline is further provided with a first clean air communication pipeline, the first clean air communication pipeline is The second cooling air intake line is connected, and the first clean air communication line is further provided with a first clean air communication control valve to control the air volume of the first clean air communication line. 如申請專利範圍第22項所述之具高溫脫附之轉輪系統，其中該第一淨氣排放管路係進一步設有一第一淨氣連通管路，該第一淨氣連通管路係與該第一冷卻氣進氣管路連接，該第一淨氣連通管路係進一步設有一第一淨氣連通控制閥門，以控制該第一淨氣連通管路的風量。 The runner system with high temperature desorption as described in Item 22 of the patent application scope, wherein the first clean air discharge pipeline is further provided with a first clean air communication pipeline, the first clean air communication pipeline is The first cooling air intake line is connected, and the first clean air communication line is further provided with a first clean air communication control valve to control the air volume of the first clean air communication line. 如申請專利範圍第22或23項所述之具高溫脫附之轉輪系統，其中該第二淨氣排放管路係進一步設有一第二淨氣連通管路，該第二淨氣 連通管路係與該第二冷卻氣進氣管路連接，該第二淨氣連通管路係進一步設有一第二淨氣連通控制閥門，以控制該第二淨氣連通管路的風量。 The runner system with high temperature desorption as described in item 22 or 23 of the patent application scope, wherein the second clean air discharge pipeline is further provided with a second clean air communication pipeline, the second clean air The communication pipeline is connected to the second cooling air intake pipeline. The second clean air communication pipeline is further provided with a second clean air communication control valve to control the air volume of the second clean air communication pipeline. 如申請專利範圍第24項所述之具高溫脫附之轉輪系統，其中該第一淨氣排放管路係進一步設有一第一淨氣第一連通管路，該第一淨氣第一連通管路係與該第一冷卻氣進氣管路連接，該第一淨氣第一連通管路係進一步設有一第一淨氣第一連通控制閥門，以控制該第一淨氣第一連通管路的風量。 The runner system with high temperature desorption as described in item 24 of the patent application scope, wherein the first clean gas discharge line is further provided with a first clean gas first communication line, the first clean gas is first The communication pipeline is connected to the first cooling gas intake pipeline, and the first clean gas first communication pipeline is further provided with a first clean gas first communication control valve to control the first clean gas The air volume of the first communication line. 如申請專利範圍第24項所述之具高溫脫附之轉輪系統，其中該第一淨氣排放管路係進一步設有一第一淨氣第二連通管路，該第一淨氣第二連通管路係與該第二冷卻氣進氣管路連接，該第一淨氣第二連通管路係進一步設有一第一淨氣第二連通控制閥門，以控制該第一淨氣第二連通管路的風量。 The runner system with high temperature desorption as described in item 24 of the patent application scope, wherein the first clean gas discharge line is further provided with a first clean gas second communication line, and the first clean gas second communication The pipeline is connected to the second cooling gas inlet pipeline, and the first clean gas second communication pipeline is further provided with a first clean gas second communication control valve to control the first clean gas second communication pipe The air volume of the road. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第一脫附濃縮氣體管路係進一步設有一風機。 The runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, wherein the first desorption concentrated gas pipeline is further provided with a fan. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第二脫附濃縮氣體管路係進一步設有一風機。 The runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, wherein the second desorption concentrated gas pipeline is further provided with a fan. 如申請專利範圍第21、22、23或24項所述之具高溫脫附之轉輪系統，其中該第二淨氣排放管路係進一步設有一風機。 For the runner system with high temperature desorption as described in items 21, 22, 23 or 24 of the patent application scope, the second clean gas discharge pipeline is further provided with a fan. 一種具高溫脫附之轉輪方法，係設有一吸附轉輪、一第一加熱裝置及一第二加熱裝置，該轉輪方法的主要步驟係包括；輸入待吸附之氣體：該吸附轉輪之吸附區的一側係由一廢氣進氣管路來輸入待吸附之氣體，而該吸附轉輪之吸附區的另一側則透過一淨氣排放 管路來輸送經過吸附後之氣體；輸入用來冷卻之氣體：該吸附轉輪之冷卻區的一側係由一冷卻氣進氣管路來輸入用來冷卻之氣體，而該吸附轉輪之冷卻區的另一側則透過一冷卻氣輸送管路來連接至該第一加熱裝置，以將經過該吸附轉輪之冷卻區的氣體輸送到該第一加熱裝置內；輸送高溫熱氣進行脫附：該吸附轉輪之脫附區的另一側係由一第一熱氣輸送管路來輸送該第一加熱裝置內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路係設有一熱氣旁通管路，透過該熱氣旁通管路連接至該第二加熱裝置，而該吸附轉輪之脫附區的一側則透過一脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；以及再將高沸點有機物脫出：該吸附轉輪之高溫脫附區的另一側係由一第二熱氣輸送管路來輸送由該第二加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該吸附轉輪之高溫脫附區的一側則透過一高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該脫附濃縮氣體管路內。 A runner method with high temperature desorption is provided with an adsorption runner, a first heating device and a second heating device. The main steps of the runner method include: inputting the gas to be adsorbed: the adsorption rotor One side of the adsorption zone is fed by an exhaust gas inlet line to the gas to be adsorbed, and the other side of the adsorption zone of the adsorption runner is discharged through a clean gas Pipeline to transport the gas after adsorption; input gas for cooling: one side of the cooling area of the adsorption runner is a cooling gas inlet line to input the gas for cooling, and the adsorption runner The other side of the cooling zone is connected to the first heating device through a cooling gas delivery line to transfer the gas passing through the cooling zone of the adsorption rotor into the first heating device; high-temperature hot gas is transferred for desorption : The other side of the desorption zone of the adsorption runner is transported by a first hot gas delivery pipeline to transport the high-temperature hot gas generated in the first heating device for desorption, and the first hot gas delivery pipeline is provided There is a hot gas bypass line connected to the second heating device through the hot gas bypass line, and one side of the desorption area of the adsorption rotor is conveyed through a desorption concentrated gas line after desorption Desorb the concentrated gas; and then remove the high-boiling organic matter: the other side of the high-temperature desorption zone of the adsorption rotor is transported by a second hot gas delivery pipeline to a certain temperature raised by the second heating device High-temperature hot gas to remove high-boiling organics (VOC), and one side of the high-temperature desorption zone of the adsorption runner is transported through the high-temperature desorption concentrated gas pipeline through a high-temperature desorption concentrated gas pipeline Into the desorbed concentrated gas pipeline. 一種具高溫脫附之轉輪方法，係設有一吸附轉輪、一第一加熱裝置及一第二加熱裝置，該轉輪方法的主要步驟係包括；輸入待吸附之氣體：該吸附轉輪之吸附區的一側係由一廢氣進氣管路來輸入待吸附之氣體，而該吸附轉輪之吸附區的另一側則透過一淨氣排放管路來輸送經過吸附後之氣體；輸入用來冷卻之氣體：該吸附轉輪之冷卻區的另一側係由一冷卻氣進氣管路來輸入用來冷卻之氣體，而該吸附轉輪之冷卻區的一側則透過一冷 卻氣輸送管路來連接至該第一加熱裝置，以將經過該吸附轉輪之冷卻區的氣體輸送到該第一加熱裝置內；輸送高溫熱氣進行脫附：該吸附轉輪之脫附區的一側係由一第一熱氣輸送管路來輸送該第一加熱裝置內所產生的高溫熱氣以進行脫附，且該第一熱氣輸送管路係設有一熱氣旁通管路，透過該熱氣旁通管路連接至該第二加熱裝置，而該吸附轉輪之脫附區的另一側則透過一脫附濃縮氣體管路來輸送經過脫附後之脫附濃縮氣體；以及再將高沸點有機物脫出：該吸附轉輪之高溫脫附區的一側係由一第二熱氣輸送管路來輸送由該第二加熱裝置內所提升到一定溫度的高溫熱氣，以將高沸點有機物(VOC)脫出，而該吸附轉輪之高溫脫附區的另一側則透過一高溫脫附濃縮氣體管路來輸送經過脫附後之高溫脫附濃縮氣體至該脫附濃縮氣體管路內。 A runner method with high temperature desorption is provided with an adsorption runner, a first heating device and a second heating device. The main steps of the runner method include: inputting the gas to be adsorbed: the adsorption rotor One side of the adsorption zone is a waste gas inlet line to input the gas to be adsorbed, and the other side of the adsorption zone of the adsorption rotor is through a clean gas discharge line to transport the adsorbed gas; input Gas to be cooled: the other side of the cooling zone of the adsorption runner is supplied with a cooling gas inlet line for cooling gas, and one side of the cooling zone of the adsorption runner is passed through a cooling The gas delivery pipeline is connected to the first heating device to deliver the gas passing through the cooling zone of the adsorption rotor to the first heating device; delivering high-temperature hot gas for desorption: the desorption zone of the adsorption rotor On one side, a first hot gas delivery pipeline is used to transport the high-temperature hot gas generated in the first heating device for desorption, and the first hot gas delivery pipeline is provided with a hot gas bypass pipeline through which the hot gas The bypass line is connected to the second heating device, and the other side of the desorption area of the adsorption runner is conveyed through a desorption concentrated gas line to the desorption concentrated gas after desorption; Boiling point organic matter extraction: One side of the high-temperature desorption zone of the adsorption rotor is transported by a second hot gas delivery line to transport high-temperature hot gas raised to a certain temperature in the second heating device to remove high-boiling point organic matter ( VOC) desorption, and the other side of the high-temperature desorption zone of the adsorption runner conveys the high-temperature desorption concentrated gas after desorption into the desorption concentrated gas pipeline through a high-temperature desorption concentrated gas pipeline . 如申請專利範圍第41或42項所述之具高溫脫附之轉輪方法，其中該脫附濃縮氣體管路的另一端係進一步與一焚燒裝置連接。 The runner method with high temperature desorption as described in item 41 or 42 of the patent application scope, wherein the other end of the desorption concentrated gas pipeline is further connected to an incineration device. 如申請專利範圍第43項所述之具高溫脫附之轉輪方法，其中該焚燒裝置係進一步為直燃式焚燒爐(TO)、觸媒爐或蓄熱式焚燒爐(RTO)之其中任一。 The runner method with high temperature desorption as described in item 43 of the patent application scope, wherein the incinerator is any one of a direct combustion incinerator (TO), a catalyst furnace or a regenerative incinerator (RTO) . 如申請專利範圍第44項所述之具高溫脫附之轉輪方法，其中該蓄熱式焚燒爐(RTO)係設有入口及出口，該入口係與該脫附濃縮氣體管路連接，該出口則連接至一煙囪。 The runner method with high temperature desorption as described in item 44 of the patent application scope, wherein the regenerative incinerator (RTO) is provided with an inlet and an outlet, the inlet is connected to the desorbed concentrated gas pipeline, the outlet It is connected to a chimney. 如申請專利範圍第41或42項所述之具高溫脫附之轉輪方法，其中該淨氣排放管路的另一端係與一煙囪連接。 The runner method with high temperature desorption as described in item 41 or 42 of the patent application scope, wherein the other end of the clean gas discharge pipe is connected to a chimney. 如申請專利範圍第41或42項所述之具高溫脫附之轉輪方法，其中該第一加熱裝置及第二加熱裝置係進一步為加熱器、管道加熱器或熱交換器之其中任一，該加熱器係採用電熱絲、電熱管或電熱片之其中任一，該管道加熱器係採用氣體燃料或液體燃料之其中任一。 The runner method with high temperature desorption as described in item 41 or 42 of the patent application scope, wherein the first heating device and the second heating device are further any one of a heater, a pipe heater or a heat exchanger, The heater adopts any one of electric heating wire, electric heating tube or electric heating sheet, and the pipeline heater adopts any one of gas fuel or liquid fuel. 如申請專利範圍第41或42項所述之具高溫脫附之轉輪方法，其中該熱氣旁通管路係進一步設有一熱氣旁通控制閥門，以控制該熱氣旁通管路的風量。 The runner method with high temperature desorption as described in item 41 or 42 of the patent application scope, wherein the hot gas bypass line is further provided with a hot gas bypass control valve to control the air volume of the hot gas bypass line. 如申請專利範圍第41項所述之具高溫脫附之轉輪方法，其中該廢氣進氣管路係進一步設有一廢氣連通管路，該廢氣連通管路係與該冷卻氣進氣管路連接，該廢氣連通管路係進一步設有一廢氣連通控制閥門，以控制該廢氣連通管路的風量。 The runner method with high temperature desorption as described in item 41 of the patent application scope, wherein the exhaust gas intake line is further provided with an exhaust gas communication line, and the exhaust gas communication line is connected with the cooling gas intake line The exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. 如申請專利範圍第42項所述之具高溫脫附之轉輪方法，其中該淨氣排放管路係進一步設有一淨氣連通管路，該淨氣連通管路係與該冷卻氣進氣管路連接，該淨氣連通管路係進一步設有一淨氣連通控制閥門，以控制該淨氣連通管路的風量。 The runner method with high temperature desorption as described in item 42 of the patent application scope, wherein the clean gas discharge pipeline is further provided with a clean air communication pipeline, the clean air communication pipeline is connected with the cooling air intake pipe Connection, the clean air communication pipeline is further provided with a clean air communication control valve to control the air volume of the clean air communication pipeline. 如申請專利範圍第41或42項所述之具高溫脫附之轉輪方法，其中該脫附濃縮氣體管路係進一步設有一風機。 The runner method with high temperature desorption as described in item 41 or 42 of the patent application scope, wherein the desorption concentrated gas pipeline is further provided with a fan. 如申請專利範圍第41或42項所述之具高溫脫附之轉輪方法，其中該淨氣排放管路係進一步設有一風機。 The runner method with high temperature desorption as described in item 41 or 42 of the patent application scope, wherein the net gas discharge pipeline is further provided with a fan. 一種具高溫脫附之轉輪系統，係包括：一吸附轉輪，該吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該一廢氣進氣管路的一端係連接至該吸附轉輪之吸附區的一側，該一淨 氣排放管路的一端係與該吸附轉輪之吸附區的另一側連接，該一冷卻氣進氣管路的一端係與該吸附轉輪之冷卻區之一側連接，該一冷卻氣輸送管路的一端係與該吸附轉輪之冷卻區的另一側連接，該一第一熱氣輸送管路的一端係與該吸附轉輪之脫附區的另一側連接，該一第二熱氣輸送管路的一端係與該吸附轉輪之高溫脫附區的另一側連接，該一脫附濃縮氣體管路的一端係與該吸附轉輪之脫附區的一側連接，該一高溫脫附濃縮氣體管路的一端係與該吸附轉輪之高溫脫附區的一側連接，該高溫脫附濃縮氣體管路的另一端係與該脫附濃縮氣體管路連接；一第一加熱裝置，該冷卻氣輸送管路的另一端係與該第一加熱裝置連接，該第一熱氣輸送管路的另一端係與該第一加熱裝置連接；以及一第二加熱裝置，該第一熱氣輸送管路係設有一熱氣旁通管路，該熱氣旁通管路的另一端係與該第二加熱裝置連接，該第二熱氣輸送管路的另一端係與該第二加熱裝置連接。 A runner system with high-temperature desorption includes: an adsorption runner, which is provided with an adsorption zone, a cooling zone, a desorption zone and a high-temperature desorption zone, and one end of the exhaust gas intake line is One side connected to the adsorption area of the adsorption rotor One end of the gas discharge line is connected to the other side of the adsorption zone of the adsorption runner, and one end of the cooling gas intake line is connected to one side of the cooling zone of the adsorption runner, the one cooling gas is conveyed One end of the pipeline is connected to the other side of the cooling zone of the adsorption runner, one end of the first hot gas delivery pipeline is connected to the other side of the desorption zone of the adsorption runner, the second hot gas One end of the conveying pipeline is connected to the other side of the high-temperature desorption zone of the adsorption runner. One end of the desorption concentrated gas pipeline is connected to one side of the desorption zone of the adsorption runner. One end of the desorption concentrated gas pipeline is connected to one side of the high-temperature desorption zone of the adsorption runner, and the other end of the high-temperature desorption concentrated gas pipeline is connected to the desorption concentrated gas pipeline; a first heating Device, the other end of the cooling gas delivery line is connected to the first heating device, the other end of the first hot gas delivery line is connected to the first heating device; and a second heating device, the first hot gas The conveying pipeline is provided with a hot gas bypass pipeline, the other end of the hot gas bypass pipeline is connected to the second heating device, and the other end of the second hot gas conveying pipeline is connected to the second heating device. 一種具高溫脫附之轉輪系統，係包括：一吸附轉輪，該吸附轉輪係設有吸附區、冷卻區、脫附區及高溫脫附區，該一廢氣進氣管路的一端係連接至該吸附轉輪之吸附區的一側，該一淨氣排放管路的一端係與該吸附轉輪之吸附區的另一側連接，該一冷卻氣進氣管路的一端係與該吸附轉輪之冷卻區之另一側連接，該一冷卻氣輸送管路的一端係與該吸附轉輪之冷卻區的一側連接，該一第一熱氣輸送管路的一端係與該吸附轉輪之脫附區的一側連接，該一第二熱氣輸送管路的一端係與該吸附轉輪之高溫脫附區的一側連接，該一脫附濃縮氣體管路的一端係與該吸附轉輪之脫附區的另一側連接，該一高溫脫附濃縮 氣體管路的一端係與該吸附轉輪之高溫脫附區的另一側連接，該高溫脫附濃縮氣體管路的另一端係與該脫附濃縮氣體管路連接；一第一加熱裝置，該冷卻氣輸送管路的另一端係與該第一加熱裝置連接，該第一熱氣輸送管路的另一端係與該第一加熱裝置連接；以及一第二加熱裝置，該第一熱氣輸送管路係設有一熱氣旁通管路，該熱氣旁通管路的另一端係與該第二加熱裝置連接，該第二熱氣輸送管路的另一端係與該第二加熱裝置連接。 A runner system with high-temperature desorption includes: an adsorption runner, which is provided with an adsorption zone, a cooling zone, a desorption zone and a high-temperature desorption zone, and one end of the exhaust gas intake line is Connected to one side of the adsorption zone of the adsorption runner, one end of the clean gas discharge line is connected to the other side of the adsorption zone of the adsorption runner, and one end of the cooling air intake line is connected to the The other side of the cooling zone of the adsorption rotor is connected, one end of the cooling gas delivery pipeline is connected to one side of the cooling zone of the adsorption rotor, and one end of the first hot gas delivery pipeline is connected to the adsorption rotor One side of the desorption zone of the wheel is connected, one end of the second hot gas delivery pipeline is connected to one side of the high-temperature desorption zone of the adsorption rotor, and one end of the desorption concentrated gas pipeline is connected to the adsorption The other side of the desorption area of the runner is connected, the high temperature desorption concentration One end of the gas pipeline is connected to the other side of the high-temperature desorption zone of the adsorption runner, and the other end of the high-temperature desorption concentrated gas pipeline is connected to the desorption concentrated gas pipeline; a first heating device, The other end of the cooling gas delivery line is connected to the first heating device, the other end of the first hot gas delivery line is connected to the first heating device; and a second heating device, the first hot gas delivery tube The road system is provided with a hot gas bypass line, the other end of the hot gas bypass line is connected to the second heating device, and the other end of the second hot gas delivery line is connected to the second heating device. 如申請專利範圍第53或54項所述之具高溫脫附之轉輪系統，其中該脫附濃縮氣體管路的另一端係進一步與一焚燒裝置連接。 The runner system with high temperature desorption as described in item 53 or 54 of the patent application scope, wherein the other end of the desorption concentrated gas pipeline is further connected to an incineration device. 如申請專利範圍第55項所述之具高溫脫附之轉輪系統，其中該焚燒裝置係進一步為直燃式焚燒爐(TO)、觸媒爐或蓄熱式焚燒爐(RTO)之其中任一。 The runner system with high temperature desorption as described in item 55 of the patent application scope, wherein the incinerator is any one of a direct combustion incinerator (TO), a catalyst furnace or a regenerative incinerator (RTO) . 如申請專利範圍第56項所述之具高溫脫附之轉輪系統，其中該蓄熱式焚燒爐(RTO)係設有入口及出口，該入口係與該脫附濃縮氣體管路連接，該出口則連接至一煙囪。 The runner system with high temperature desorption as described in item 56 of the patent application scope, wherein the regenerative incinerator (RTO) is provided with an inlet and an outlet, the inlet is connected to the desorbed concentrated gas pipeline, the outlet It is connected to a chimney. 如申請專利範圍第53或54項所述之具高溫脫附之轉輪系統，其中該淨氣排放管路的另一端係與一煙囪連接。 The runner system with high temperature desorption as described in item 53 or 54 of the patent application scope, wherein the other end of the net gas discharge pipe is connected to a chimney. 如申請專利範圍第53或54項所述之具高溫脫附之轉輪系統，其中該第一加熱裝置及第二加熱裝置係進一步為加熱器、管道加熱器或熱交換器之其中任一，該加熱器係採用電熱絲、電熱管或電熱片之其中任一，該管道加熱器係採用氣體燃料或液體燃料之其中任一。 The runner system with high temperature desorption as described in item 53 or 54 of the patent application scope, wherein the first heating device and the second heating device are further any one of a heater, a pipe heater or a heat exchanger, The heater adopts any one of electric heating wire, electric heating tube or electric heating sheet, and the pipeline heater adopts any one of gas fuel or liquid fuel. 如申請專利範圍第53或54項所述之具高溫脫附之轉輪系統，其中該熱氣旁通管路係進一步設有一熱氣旁通控制閥門，以控制該熱氣旁通管路的風量。 The runner system with high temperature desorption as described in item 53 or 54 of the patent application scope, wherein the hot gas bypass line is further provided with a hot gas bypass control valve to control the air volume of the hot gas bypass line. 如申請專利範圍第53項所述之具高溫脫附之轉輪系統，其中該廢氣進氣管路係進一步設有一廢氣連通管路，該廢氣連通管路係與該冷卻氣進氣管路連接，該廢氣連通管路係進一步設有一廢氣連通控制閥門，以控制該廢氣連通管路的風量。 The runner system with high temperature desorption as described in item 53 of the patent application scope, wherein the exhaust gas intake line is further provided with an exhaust gas communication line which is connected to the cooling air intake line The exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. 如申請專利範圍第54項所述之具高溫脫附之轉輪系統，其中該淨氣排放管路係進一步設有一淨氣連通管路，該淨氣連通管路係與該冷卻氣進氣管路連接，該淨氣連通管路係進一步設有一淨氣連通控制閥門，以控制該淨氣連通管路的風量。 The runner system with high temperature desorption as described in item 54 of the patent application scope, wherein the clean gas discharge pipeline is further provided with a clean air communication pipeline, the clean air communication pipeline is connected with the cooling air intake pipe Connection, the clean air communication pipeline is further provided with a clean air communication control valve to control the air volume of the clean air communication pipeline. 如申請專利範圍第53或54項所述之具高溫脫附之轉輪系統，其中該脫附濃縮氣體管路係進一步設有一風機。 The runner system with high temperature desorption as described in item 53 or 54 of the patent application scope, wherein the desorption concentrated gas pipeline is further provided with a fan. 如申請專利範圍第53或54項所述之具高溫脫附之轉輪系統，其中該淨氣排放管路係進一步設有一風機。 The runner system with high temperature desorption as described in item 53 or 54 of the patent application scope, wherein the net gas discharge pipeline is further provided with a fan.
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TWI821714B (en) * 2021-07-20 2023-11-11 華懋科技股份有限公司 Carbon dioxide adsorption runner system and method thereof
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6294000B1 (en) * 1999-09-24 2001-09-25 Durr Environmental, Inc. Rotary concentrator and method of processing adsorbable pollutants
CN1089262C (en) * 1999-06-11 2002-08-21 华懋科技股份有限公司 Method of raising the efficiency of runner type adsorption system in eliminating volatile organic waste gas
EP1683563A2 (en) * 2005-01-21 2006-07-26 POLARIS Srl Method and system for treating a gaseous stream containing organic and inorganic volatile compounds
CN101827640A (en) * 2007-09-12 2010-09-08 蒙特斯公司 Apparatus and method for in-situ high temperature regeneration of a rotor sorption concentrator
TW201238653A (en) * 2011-03-25 2012-10-01 Jg Environmental Tech Co Ltd Improved on-line regeneration device and method for zeolite rotor concentrator
TW201819028A (en) * 2017-02-03 2018-06-01 傑智環境科技股份有限公司 High efficiency purification system and method using series-connected rotary wheels

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5512083A (en) * 1993-10-25 1996-04-30 Uop Process and apparatus for dehumidification and VOC odor remediation
WO2012147153A1 (en) * 2011-04-26 2012-11-01 株式会社西部技研 Adsorption dehumidifier
CN105771639B (en) * 2016-05-10 2018-02-23 西部技研环保节能设备（常熟）有限公司 Air cleaning unit is polluted using the low concentration VOC of catalyst runner
CN108452637B (en) * 2017-02-17 2020-05-05 杰智环境科技股份有限公司 Serial-type rotating wheel high-efficiency purification system and serial-type rotating wheel high-efficiency purification method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1089262C (en) * 1999-06-11 2002-08-21 华懋科技股份有限公司 Method of raising the efficiency of runner type adsorption system in eliminating volatile organic waste gas
US6294000B1 (en) * 1999-09-24 2001-09-25 Durr Environmental, Inc. Rotary concentrator and method of processing adsorbable pollutants
EP1683563A2 (en) * 2005-01-21 2006-07-26 POLARIS Srl Method and system for treating a gaseous stream containing organic and inorganic volatile compounds
CN101827640A (en) * 2007-09-12 2010-09-08 蒙特斯公司 Apparatus and method for in-situ high temperature regeneration of a rotor sorption concentrator
TW201238653A (en) * 2011-03-25 2012-10-01 Jg Environmental Tech Co Ltd Improved on-line regeneration device and method for zeolite rotor concentrator
TW201819028A (en) * 2017-02-03 2018-06-01 傑智環境科技股份有限公司 High efficiency purification system and method using series-connected rotary wheels

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